CA1313755C - Oil recovery process using alkyl hydroxyaromatic dianionic surfactants as mobility control agents - Google Patents
Oil recovery process using alkyl hydroxyaromatic dianionic surfactants as mobility control agentsInfo
- Publication number
- CA1313755C CA1313755C CA000579493A CA579493A CA1313755C CA 1313755 C CA1313755 C CA 1313755C CA 000579493 A CA000579493 A CA 000579493A CA 579493 A CA579493 A CA 579493A CA 1313755 C CA1313755 C CA 1313755C
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/58—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
- C09K8/594—Compositions used in combination with injected gas, e.g. CO2 orcarbonated gas
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/58—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
- C09K8/584—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids characterised by the use of specific surfactants
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/58—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
- C09K8/592—Compositions used in combination with generated heat, e.g. by steam injection
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
- E21B43/24—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
Abstract
ABSTRACT
A method for recovering oil from a subterranean formation is disclosed wherein an aqueous surfactant solution is injected into the formation to reduce the mobility of gas in a gas-flooding process.
The gas may include hydrocarbon gas, inert gas, carbon dioxide, and steam. The surfactant is represented by the general formula where R is a linear or branched chain alkyl group with n carbon atoms wherein n ranges from 0 to about 18, except that if the gas is steam n ranges from about 9 to about 30;
x ranges from 0 to about 20 and y ranges from 0 to about 20, provided x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 0 to 4, except that if the gas is steam m ranges from 1 to 4, with the proviso that the sum of x + y + m is at least one; and each M is a cation.
A method for recovering oil from a subterranean formation is disclosed wherein an aqueous surfactant solution is injected into the formation to reduce the mobility of gas in a gas-flooding process.
The gas may include hydrocarbon gas, inert gas, carbon dioxide, and steam. The surfactant is represented by the general formula where R is a linear or branched chain alkyl group with n carbon atoms wherein n ranges from 0 to about 18, except that if the gas is steam n ranges from about 9 to about 30;
x ranges from 0 to about 20 and y ranges from 0 to about 20, provided x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 0 to 4, except that if the gas is steam m ranges from 1 to 4, with the proviso that the sum of x + y + m is at least one; and each M is a cation.
Description
137~
OIL RECOVERY PROCESS
USING ALKYL ~YDROXYAROMATIC DIANIONIC SURFACTANTS
AS MOBILITY CONTROL AGENTS
Field of the Invention This invention relates to recovering oil from a subterranean oil-bearing formation by injecting into the formation a gas and an aqueous surfactant solution to control gas mobility. More specifically, the invention pertains to use of alkyl hydroxyaromatic dianionic surfactants to reduce gas mobility within an oil-bearing formation.
Back~round of the Invention A significant fraction of the oil-in-place is left in the ground after primary or secondary recovery. Gas injection, sometimes referred to as gas flooding, has been used to recover this remaining oil. The terms "gas injection" and "gas flooding" as used herein will mean an oil recovery process in which the fluid injected is a hydrocarbon gas, inert gas, carbon dioxide, or steam.
The success of gas floods has been diminished by the unfavorable mobility ratio between the gas and oil. The viscosities of gas mixtures are often 10 to 100 times lower than oil and water viscosities. At these unfavorable viscosity ratios, ga6es finger and channel through the formation, leaving parts of the reservoir -2- 1~13~
unswept. Added to this fingering is the inherent tendency of a highly mobile gas to flow preferentially through the more permeable rock 6ections or to gravity override in the reservoir. These basic factors --permeability variations and unfavorable mobility and density ratios-- greatly reduce the effectiveness of gas floods and may make them uneconomic. One apparent remedy is to control the mobility of the injected gas.
It has been suggested that the mobility of the gas may be reduced by injecting into a formation or forming in situ a mixture of a gas and an aqueous surfactant solution. Such mixtures are commonly referred to as foams. Since the effective viscosity of foam is greater than the viscosity of its components, it has been suggested that such mixtures of gas and aqueous surfactant solution will help improve the sweep efficiency of gas drives.
Foam is a dispersion of a large volume of gas in a relatively small volume of liquid. It should be noted, however, that at reservoir conditions several gases, including C02, exist as a dense fluid, resembling a liquid more than a gas. For this reason, the term "solvent" is sometimes used to describe the "gas" and the term "emulsion" is 60metimes used to describe the solvent-water mixture.
Mobility control may be accomplished by injecting a bank of aqueous surfactant solution followed by injecting gas. Alternatively, banks of surfactant solution can be interspersed with the gas during injection to achieve a more continuous effect.
_3_ 1 31 37~5 It is known that the choice of surfactant for use as a mobility control a8ent is of vital importance. Many surfactants cause too severe a reduction of gas mobility, thus making the gas difficult to inject into the reservoir. Other surfactants cause an insufficient reduction of gas mobility, thus leading to inadequate improvement of sweep efficiency.
Conditions existing in a typical oil reservoir impose a severe challenge to surfactant performance. Most reservoirs have an aqueous phase of brine that may vary in concentration from 0.5% to 15%
NaCl. Also, there may be divalent ions such as Ca and Mg++
present in significant concentrations (100 ppm or more). Adsorption or trapping of surfactant in viscous emulsions is another limitation.
The effect of crude oil and temperature can also be deleterious if not properly taken into consideration.
Considerable effort has been made by the petroleum industry to identify surfactants with proper chemical stability, adsorption characteristics, and capability for gas-mobility reduction. Hundreds of surfactants have been screened. There continues to be a significant need, however, for improved gas mobility-control processes in which the amount of additional oil recovered as a result of in~ecting the surfactant and gas is sufficient to ~ustify the cost of the process.
-4- 131375~
Summary of the Invention The present invention relates to an improved process for -reducing gas mobility in a region of 8 subterranean, oil-containing formation by introducing into the formation a gas and an aqueous solutio~ conta~ning a surfactant characterized by the formula R~O[CH2CH(cH3)0]ylcH2cH2o]yR~so3M
where R i8 a linear or branched chain alkyl group with n carbon atoms wherein n ranges from 0 to about 18, except that if the gas is steam n ranges from about 9 to about 30;
x ranges from 0 to about 20 and y ranges from 0 to about 20, provided x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 0 to 4, except that if the gas is steam m ranges from 1 to 4, with the proviso that the sum of x + y + m is at least one; and each M+ is a cation.
In a preferred embodiment for reducing the mobility of carbon dioxide, hydrocarbon gas, or inert gas, the aqueous solution contains 0.02 to 1.0~ by weight C6 18 phenol disulfonate contain~ng 0-6 ethoxy groups terminated by an ethyl or a propyl sùlfonate group. A
preferred surfactant for a steam flood is C12 30 phenol disulfonate containing 0-6 ethoxy groups terminated by an ethyl or propyl sulfonate group.
13~rl~
The gas mobility is reduced in situ in the formation by injecting the aqueous surfactant solution into the formation through an injection well and injecting gas into the formation through the in3ection well with or after injection of the aqueous surfactant S solution. In another embodiment the formation is first flooded with gas before injecting the mobility control agent. The steps of injecting aqueous surfactant solution and gas may be repeated.
The practice of this invention provides effective mobility control for gas floods and improves oil displacement efficiency.
Brief Description of the Drawin~s FIGURE 1, which illustrates the result of an experimental core displacement test, plots comparative mobility of a mixture of C2 and aqueous surfactant solution generated in accordance with this invention as a function of pore volumes of C02 injected.
Detailed Description of the Invention A mobility control system comprising a mixture of gas and an aqueous solution containing a surfactant for use as a mobility control fluid in recovering oil from a subterranean oil-bearing formation should ideally have the following characteristics:
The mixture should provide resistance to flow of the gas in gas-swept zones where the oil saturation is low.
The mixture should not impair the mobility of gas and oil in unswept zones where oil saturation is high.
-6- 13137~5 The 6urfactant retention should be low and the surfactant should be effective at low concentrations. - --- -- The properties of the mixture should be insensitive to reasonable variations in reservoir salinity, temperature, and surfactant concentration.
The present invention is premised on the discovery that a mobility control system exhibiting the beneficial characteristics listed above can be formed by use of a surfactant characterized by the formula R~,O[CH2CH~CH3)0]xtC}{2C~20]yR~S03~1 (1) where R i8 a linear or branched chain alkyl group with n carbon atoms wherein n ranges from 0 to about 18, except that if the gas is steam n ranges from about 9 to about 30;
x ranges from 0 to about 20 and y ranges from 0 to about 20, provided x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 0 to 4, except that if the gas is steam ~ ~ m ranges from 1 to 4, with the proviso that the sum of ;~ x + y + m is at least one; and each M+ is a cation.
The ethoxy and propoxy groups may be present as a block co-polymer chain or they may be intermixed within the alkoxy chain.
1313~5 M can include alkali metals such as sodium, potassium and lithium, alkaline earth metals such as calcium and barium, amines including alkanol amines and their oxyalkylated adduct~j and ammonium.
It should be understood the polyalkoxy surfactants used in the present invention will not normally be pure substances in the strict sense, but a mixture of components such that x and y are the resulting average values. It should also be understood that in the preparation of the surfactants used in the present invention, the surfactant formulation may contain compounds falling outside formula (1). For example~ the formulation may include small amounts of compound6 containing more than one alkyl group or more than one sulfonate group attached to the benzene ring. The formulation may also include small amounts of monosulfonate in which either sulfonate group in formula (1) is absent.
, ~
-8- 13~3~5~
Non-limiting examples of surfactants characterized by formula (1) suitable for reducing the mobility of carbon dioxide, hydrocarbon gas and inert gas are listed in Table 1:
R R' x y M
linear C16H33 CH2CH2CH2 o Na+
branched CgHlg CH2CH2 2 Na+
linear C16H33 CH(cH3)cH2cH2 0 0 Na+
branched CgHlg none 0 3 Na+
branched CgHlg CH2CH2 1 3 Na+
branched CgHlg CH2CH2 3 0 Na+
+
branched CgHlg CH2CH2 2 NH4 Non-limiting examples of surfactants characterized by formula (1) suitable for reducing mobility of steam are listed in Table 2.
+
R R' x v M
linear C18H37 CH2CH2CH2 0 Na+
branched C12H23 CH2CH2 2 Na+
linear C18H37 CH(CH3)CH2CH2 0 Na+
linear C18H37 CH2CH2 1 3 Na+
linear C18H37 CH2CH2 3 0 Na~
linear C18H37 CH2CH2 0 2 NH4 g 13~3~5 In selecting mobility control surfactants of this invention for a particular 100ding operation, the effect~ of gas composition should be-considered. A mobility control sy6tem comprising a surfactant represented by formula (l) above and steam will generally have higher mobility than a mobility control system comprising the same surfactant and other gases such as C02 and N2. Since the mobility of gas in this invention tends to decrease as the number of carbon atoms of the lipophile portion of the surfactant increases, the number of carbon atoms of R in formula (l) is generally higher for use in steam floods than the number of carbon atoms of R for use in other gas floods.
Referring again to formula (1), when m = 0, the R' alkyl group is absent, and the surfactant contains a sulfate group. It is well known to those skilled in the art that sulfate surfactants are susceptible to rapid chemical degradation by hydrolysis of the sulfate group at high temperature and/or low pH. The product of the degradation reaction tends to be less effective as a mobility-reducing agent, and may have significantly higher retention than the original surfactant.
For this reason, surfactants having m = 0 would generally not be used in flooding processes where the temperature is high, such as steam flooding, or where pH is low, such as C02 flooding. Surfactants having m = 0 may, however, be used under conditions where the rate of hydrolysis of the sulfate group is low. Examples of such conditions may include hydrocarbon or inert gas flooding at low temperature, or C02 flooding at low temperature in a reservoir where pH is buffered by reservoir minerals to a level at which hydrolysis ~ 8 acceptably slow.
-lo- 13137~
Particularly preferred mobility control systems of this inventian include surfactants having a composition characterized by the formula ~ --R ~ O(CH2CH20)yR'S03M (2) where: R is a C6 to C18 linear or branched alkyl chain for use in C02, inert gas, and hydrocarbon gas floods, and R is a linear or branched C12 to C30 alkyl chain for use in steam floods; y i6 0 to 6; R' is an alkyl group containing two or three carbons; and each M is an alkali metal ion.
As understood by those skilled in the art, the optimum surfactant for a particular gas flooding process will depend on the reservoir in which it is used. The optimum values of n, m, x, and y in formula (1) for a particular gas flooding operation will depend on the reservoir conditions of temperature, pressure, permeability, salinity, oil composition, and the like. The optimum surfactant maybe determined by performing core displacement tests using procedures known to those skilled in the art. Such tests may be used to select a surfactant that has low retention, can be used at low concentration, provides a substantial but not excessive reduction of gas mobility, and does not impair the recovery of the oil.
The surfactants of the present invention may be prepared by known procedures. The following is a description of one way of -ll- 1 3 ~
preparing such surfactants. For those surfactants having two or more carbon atoms attached to the benzene ring, the synthesis procedure usually begins by reacting phenol with olefins at temperatures and pressures sufficient to alkylate the phenol. The reaction is conducted in the presence of an effective amount of an acid catalyst such as boron triflouride, sulfuric acid, phosphoric acid, or sulfonic acid. The alkyl phenols may then be reacted with alkylene oxides in the presence of a base to provide alkyl-phenyl polyalkoxy alcohols.
The alkoxy derivatives may then be reacted with a sultone such as propane sultone or butane sultone to form an alkyl phenol alkoxy monosulfonate. A sulfonate group may be added on the aromatic ring to produce a disulfonate by sulfonating the alkyl phenol alkoxy monosulfonate product with a suitable sulfonating agent such as chlorosulfonic acid. The disulfonic acid may then be neutralized with a base such as 50% NaOH.
The present invention is useful where it is desirable to reduce gas mobility in an area of a subterranean, oil-containing formation to facilitate production of oil from or displacement of oil through the pores of the formation. The formation may be any light or heavy oil reservoir having a permeability suitable for an application of a fluid to displace oil away from a well borehole in a well-cleaning operation or to displace oil through the formation to a producing location in an oil recovery operation.
In general, the gaseous fluids can comprise steam, carbon dioxide, inert gases such as air and nitrogen, hydrocarbons such as methane, ethane, propane, and natural gas, and mixtures thereof.
-12~ 3~
Gas and aqueous surfactant solution may be-in~e~ted ineo the formation in the form of alternating banks. The gas and aqueous surfactant solution will mix in the format;on. However, where desirable, the gas and aqueous solution may be injected simultaneously, as a dispersion of the gas in the liquid or as a pair of co-flowing streams of the two fluids within a common conduit. The components are preferably injected at a pressure sufficient to displace the oil without fracturing the reservoir. However, in low permeability reservoirs controlled fractures of limited extent may be required to obtain adequate injectivity.
In the practice of one embodiment of this invention, C02 is injected into an oil-bearing subterranean formation through an injection well. The highly mobile gas will tend to flow preferentially through the more permeable rock sections. The C02 mobilizes the recoverable oil in those sections. Gas injection continues until sufficient gas has been injected to ensure recovery of a substantial portion of the oil in the more permeable zones, or until gas breakthrough occurs at the production well which is spaced apart from the injection well. A bank of brine containing a surfactant characterized by formula (1) above is then injected, followed by a second bank of C02. The surfactant solution will preferentially enter the more permeable zones and will reduce gas mobility in those areas, thus diverting C02 to previously unswept zones of the formation. Banks of surfactant solution may be alternated with banks of C02. Optionally, the composition of surfactant in the aqueous solution may be varied from one bank to the next to optimize the process. If desired, a bank of drive fluid may be injected after the -13- 1~13755 last C02 bank has been injected to displace the C02 through the formation. -- ~-In another embodiment of this invention, a small amount of surfactant characterized by formula (1) above is added to water duringthe last stage of a waterflood operation. Surfactant is injected before start-up of a gas injection project to avoid time delays associated with injecting an additional surfactant bank after the usual waterflood operation has been completed.
The process of this invention may be applied to a 6ubterranean, oil-containing formation penetrated by at least one injection well and at least one spaced-apart production well. The injection well is perforated or other fluid flow communication is established between the well and the formation. The production well is completed in fluid communication with a substantial portion of the vertical thickness of the formation. While recovery of the type contemplated by this invention may be carried out with only two wells, this invention is not limited to any particular number of wells. The invention may be practiced using a variety of well patterns as is well known in the art of oil recovery, such as a repeated five-spot pattern in which each injection well is surrounded with four production wells, or in a line-drive arrangement in which a series of aligned injection wells and a series of aligned production wells are utilized.
This process can also be used in "huff and puff" operations through a single well. In the huff and puff procedure, the reduced gas mobility is generated through the same well that is subsequently -14- i3137~
used for production. The reduced gas mobility improves the injection profile. The gas bility in swept zones is greatly reduced so the gas will invade the previously unswept tighter ~ones. The well may be shut in for a period of time before placing it on the production cycle. After the production cycle, additional cycles of injection and production can be utilized.
The aqueous surfactant solution used in this invention may be prepared from brine or carbonated water. Preferably the water available at the injection well site, often formation brine, will be used to prepare the aqueous surfactant solution.
The concentration of surfactant in the aqueous solution will ordinarily range from about 0.01 to 2% by weight and preferably from about 0.05 to 1%, and still more preferably from 0.05 to 0.5%.
As known to those skilled in the art, the volumes required for the banks of aqueous solution and gas are different for different reservoirs, but it can be estimated by known proccdures with reasonable accuracy. Generally, the total pore volume of surfactant solution used in this invention will range from 0.01 to l and preferably from 0.1 to 0.5 pore volume.
C2 used in this invention can be obtained from any ; 25 available source. It is not necessary that it be pure. The C02 that is produced through the production wells can be separated therefrom and reinjected into the formation. Recycling methods for C2 are generally known and do not need further explanation.
-1S- ~ 7 ~ ~
Steam used in the present invention can be generated as a dry, superheatedj or wet steam and subsequently mixed with aqueous liquid. The steam can be generated at surface or downhole locations and mixed with the aqueous surfactant solution at surface or downhole locations. Optionally, the steam may include a gas that is noncondensable at reservoir temperature and pressure.
Experimental Results This invention is further illustrated by the following laboratory experiments, which demonstrate the operability of the invention. The experiments are not intended as limiting the scope of the invention as defined in the appended claims.
All of the core flooding laboratory experiments described below used 1 in. X 1 in. X 12 in. (2.54cm X 2.54cm X 30.5cm) Berea sandstone cores. Differential pressures were monitored between inlet and outlet and between three pairs of taps 1 in. (2.54 cm) apart located 2 in. (5.04 cm), 6 in. (15.24 cm) and 10 in. (25.40 cm) from the inlet. All experiments were carried out at 2000 psi (13,789 kPa) with decane as the oil phase. Two high-salinity brines were used:
; 3.5% and 7.0% by weight total dissolved solids (TDS). Both brines had high contents of divalent ions, with a weight-ratio of CaC12 to NaCl of 1 to 4. Two temperatures were used: 100F (37.8C) and 150F
(65.6C). Five corefloods are discu66ed below in detail. All of the cores were flooded with oil (decane) to connate water saturation and then waterflooded with brine at a rate of 3 ft/day (0.91 m/day) prior to carrying out the experiments. Decane was completely miscible with -16- 1~13~
C2 at the conditions o the tests. The injection rate~of C~2-through the cores was 1 ft/day (0.30 m/day) and the injection rate of surfactant solution was 3 ft/day (0.91 m/day). At this rate, no oil was produced when only surfactant solution flowed through the cores.
Table 3 below sets forth core permeability, brine concentration, temperature, and injection sequence for each run.
Berea Core Permea- Brine, Temp., Run bility TDS C Iniection Sequence 1 450 md 3.5% 37.8 C2 Flood 2 550 md 3.5~ 37.8 0.1~ Surfactant, then 3 530 md 7.0~ 37.8 0.1% Surfactant, then 4 650 md 3.5% 65.6 0.1~ Surfactant, then 520 md 3.52 37.8 0.5% Surfactant, then The surfactant in runs 2-5 was a linear C16 alkyl phenol disulfonate (C16APDS), a surfactant represented by formula (1) above where x = 0, y = 0, and m = 3.
The active surfactant contained 92% disulfonate and 8%
monosulfonate. The monosulfonate component had the sulfonate group on the aromatic ring.
-17- 1313~
The objectives of the tests were to reduce C0z mobility in a core containing waterflood residual oil- and displace the residual oil with the C02. In all of the core floods in which surfactant was injected, C02 mobility was reduced by an unsteady-state process -involving a two step injection sequence: injection of surfactantsolution followed by injection of C02. In runs 2-5, sufficient surfactant solution was injected so that the effluent surfactant concentration nearly reached the influent surfactant concentration prior to injection of C02.
The comparative mobility, oil recovery and surfactant retention of each run are summarized in Table 4 below. The comparative mobility i8 defined as the ratio of the mobility of the gas-aqueous surfactant solution mixture to water mobility at residual oil saturation. At 2.0 pore volumes of C02 injection, the mobility of the aqueous phase is extremely low, so that for good approximation the comparative mobility is simply the mobility of C02. A
comparative mobility greater than unity indicates the gas will be more mobile than water at residual oil saturation. Generally, for effective mobility control in C02 floods, the comparative mobility should be below about 1, depending on field conditions. A comparative mobility above about 1 would not be desirable due to instability at the displacement front resulting in fingering, bypassing and low displacement efficiency. However, any reduction of mobility brought about by the injection of surfactant solution of this invention will be beneficial, even if the comparative mobility somewhat exeeds 1.
-18- 13137~S
. .
RUN OIL SAlVRA- SURFACTANT OIL COMPARA--TION BEFORE RETENTION RECOVERY TIVE
SURFACTANT at 1.2 M08ILIl~Y
INJECTION PV C02 at 2.0 PV
TION JECTION
mg/g rock ~ Sor .
1 0.34 _ 80 2 0.440.18 76 0.2 3 0.420.22 82 0.4 4 0.490.17 85 0.3 0.490.20 80 0.25 C2 Flood (No Surfactant) - Run 1 Run 1 provided a base case for the other runs. The comparative mobility of C02 characteristically increased to 10 after C2 breakthrough. The high mobility i8 related to the low viscosity of CO2, about 0.06 cp at 2000 psi (13,789 kPa) and 100F (37.8C).
The oil recovery was about 80% of waterflood residual oil saturation (Sor) after 1.2 pore volumes of C02 were injected.
Mobility Control Process in Waterflooded Core - Run 2 `:
An aqueous solution containing 3.5% total dissolved solids and 0.1% C16APDS was injected into a waterflooded core. No additional oil was removed from the core during injection of over 3 pore volumes of the surfactant solution. During the subsequent CO2 injection, CO2 mobility was much lower than in Run 1. As shown in FIGURE l, the comparative mobility dropped gradually, leveling off at about 0.2 after 2PV of CO2 injection.
~ 3 ~
--lg--The oil recovery at-1.2 pore volumes of C02 injected was 76Z of waterflood residual oil ~S ~, similar to that o~tained in Run 1.
Effect of Salinity, Temperature and Surfactant concentration - Runs 3, 4, and 5 Runs 3, 4, and 5 were similar to Run 2 except that the brine was more saline in Run 3, the temperature was higher in Run 4, and the surfactant concentration was greater in Run 5.
Despite the large changes in conditions, neither surfactant retention, oil recovery, nor comparative mobility was significantly different from the values obtained in Run 2, as shown in Table 4.
These results suggest that the performance of a gas mobility control process using the surfactants of this invention is relatively insensitive to reasonable variations in salinity, temperature, and surfactant concentration.
The principle of the invention and the best mode contemplated for applying that principle have been described. It will be apparent to those skilled in the art that various changes ~ay be made to the embodiments described above without departing from the spirit and scope of this invention as defined in the following claims. It is, therefore, to be understood that this invention is not limited to the specific details shown and described.
OIL RECOVERY PROCESS
USING ALKYL ~YDROXYAROMATIC DIANIONIC SURFACTANTS
AS MOBILITY CONTROL AGENTS
Field of the Invention This invention relates to recovering oil from a subterranean oil-bearing formation by injecting into the formation a gas and an aqueous surfactant solution to control gas mobility. More specifically, the invention pertains to use of alkyl hydroxyaromatic dianionic surfactants to reduce gas mobility within an oil-bearing formation.
Back~round of the Invention A significant fraction of the oil-in-place is left in the ground after primary or secondary recovery. Gas injection, sometimes referred to as gas flooding, has been used to recover this remaining oil. The terms "gas injection" and "gas flooding" as used herein will mean an oil recovery process in which the fluid injected is a hydrocarbon gas, inert gas, carbon dioxide, or steam.
The success of gas floods has been diminished by the unfavorable mobility ratio between the gas and oil. The viscosities of gas mixtures are often 10 to 100 times lower than oil and water viscosities. At these unfavorable viscosity ratios, ga6es finger and channel through the formation, leaving parts of the reservoir -2- 1~13~
unswept. Added to this fingering is the inherent tendency of a highly mobile gas to flow preferentially through the more permeable rock 6ections or to gravity override in the reservoir. These basic factors --permeability variations and unfavorable mobility and density ratios-- greatly reduce the effectiveness of gas floods and may make them uneconomic. One apparent remedy is to control the mobility of the injected gas.
It has been suggested that the mobility of the gas may be reduced by injecting into a formation or forming in situ a mixture of a gas and an aqueous surfactant solution. Such mixtures are commonly referred to as foams. Since the effective viscosity of foam is greater than the viscosity of its components, it has been suggested that such mixtures of gas and aqueous surfactant solution will help improve the sweep efficiency of gas drives.
Foam is a dispersion of a large volume of gas in a relatively small volume of liquid. It should be noted, however, that at reservoir conditions several gases, including C02, exist as a dense fluid, resembling a liquid more than a gas. For this reason, the term "solvent" is sometimes used to describe the "gas" and the term "emulsion" is 60metimes used to describe the solvent-water mixture.
Mobility control may be accomplished by injecting a bank of aqueous surfactant solution followed by injecting gas. Alternatively, banks of surfactant solution can be interspersed with the gas during injection to achieve a more continuous effect.
_3_ 1 31 37~5 It is known that the choice of surfactant for use as a mobility control a8ent is of vital importance. Many surfactants cause too severe a reduction of gas mobility, thus making the gas difficult to inject into the reservoir. Other surfactants cause an insufficient reduction of gas mobility, thus leading to inadequate improvement of sweep efficiency.
Conditions existing in a typical oil reservoir impose a severe challenge to surfactant performance. Most reservoirs have an aqueous phase of brine that may vary in concentration from 0.5% to 15%
NaCl. Also, there may be divalent ions such as Ca and Mg++
present in significant concentrations (100 ppm or more). Adsorption or trapping of surfactant in viscous emulsions is another limitation.
The effect of crude oil and temperature can also be deleterious if not properly taken into consideration.
Considerable effort has been made by the petroleum industry to identify surfactants with proper chemical stability, adsorption characteristics, and capability for gas-mobility reduction. Hundreds of surfactants have been screened. There continues to be a significant need, however, for improved gas mobility-control processes in which the amount of additional oil recovered as a result of in~ecting the surfactant and gas is sufficient to ~ustify the cost of the process.
-4- 131375~
Summary of the Invention The present invention relates to an improved process for -reducing gas mobility in a region of 8 subterranean, oil-containing formation by introducing into the formation a gas and an aqueous solutio~ conta~ning a surfactant characterized by the formula R~O[CH2CH(cH3)0]ylcH2cH2o]yR~so3M
where R i8 a linear or branched chain alkyl group with n carbon atoms wherein n ranges from 0 to about 18, except that if the gas is steam n ranges from about 9 to about 30;
x ranges from 0 to about 20 and y ranges from 0 to about 20, provided x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 0 to 4, except that if the gas is steam m ranges from 1 to 4, with the proviso that the sum of x + y + m is at least one; and each M+ is a cation.
In a preferred embodiment for reducing the mobility of carbon dioxide, hydrocarbon gas, or inert gas, the aqueous solution contains 0.02 to 1.0~ by weight C6 18 phenol disulfonate contain~ng 0-6 ethoxy groups terminated by an ethyl or a propyl sùlfonate group. A
preferred surfactant for a steam flood is C12 30 phenol disulfonate containing 0-6 ethoxy groups terminated by an ethyl or propyl sulfonate group.
13~rl~
The gas mobility is reduced in situ in the formation by injecting the aqueous surfactant solution into the formation through an injection well and injecting gas into the formation through the in3ection well with or after injection of the aqueous surfactant S solution. In another embodiment the formation is first flooded with gas before injecting the mobility control agent. The steps of injecting aqueous surfactant solution and gas may be repeated.
The practice of this invention provides effective mobility control for gas floods and improves oil displacement efficiency.
Brief Description of the Drawin~s FIGURE 1, which illustrates the result of an experimental core displacement test, plots comparative mobility of a mixture of C2 and aqueous surfactant solution generated in accordance with this invention as a function of pore volumes of C02 injected.
Detailed Description of the Invention A mobility control system comprising a mixture of gas and an aqueous solution containing a surfactant for use as a mobility control fluid in recovering oil from a subterranean oil-bearing formation should ideally have the following characteristics:
The mixture should provide resistance to flow of the gas in gas-swept zones where the oil saturation is low.
The mixture should not impair the mobility of gas and oil in unswept zones where oil saturation is high.
-6- 13137~5 The 6urfactant retention should be low and the surfactant should be effective at low concentrations. - --- -- The properties of the mixture should be insensitive to reasonable variations in reservoir salinity, temperature, and surfactant concentration.
The present invention is premised on the discovery that a mobility control system exhibiting the beneficial characteristics listed above can be formed by use of a surfactant characterized by the formula R~,O[CH2CH~CH3)0]xtC}{2C~20]yR~S03~1 (1) where R i8 a linear or branched chain alkyl group with n carbon atoms wherein n ranges from 0 to about 18, except that if the gas is steam n ranges from about 9 to about 30;
x ranges from 0 to about 20 and y ranges from 0 to about 20, provided x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 0 to 4, except that if the gas is steam ~ ~ m ranges from 1 to 4, with the proviso that the sum of ;~ x + y + m is at least one; and each M+ is a cation.
The ethoxy and propoxy groups may be present as a block co-polymer chain or they may be intermixed within the alkoxy chain.
1313~5 M can include alkali metals such as sodium, potassium and lithium, alkaline earth metals such as calcium and barium, amines including alkanol amines and their oxyalkylated adduct~j and ammonium.
It should be understood the polyalkoxy surfactants used in the present invention will not normally be pure substances in the strict sense, but a mixture of components such that x and y are the resulting average values. It should also be understood that in the preparation of the surfactants used in the present invention, the surfactant formulation may contain compounds falling outside formula (1). For example~ the formulation may include small amounts of compound6 containing more than one alkyl group or more than one sulfonate group attached to the benzene ring. The formulation may also include small amounts of monosulfonate in which either sulfonate group in formula (1) is absent.
, ~
-8- 13~3~5~
Non-limiting examples of surfactants characterized by formula (1) suitable for reducing the mobility of carbon dioxide, hydrocarbon gas and inert gas are listed in Table 1:
R R' x y M
linear C16H33 CH2CH2CH2 o Na+
branched CgHlg CH2CH2 2 Na+
linear C16H33 CH(cH3)cH2cH2 0 0 Na+
branched CgHlg none 0 3 Na+
branched CgHlg CH2CH2 1 3 Na+
branched CgHlg CH2CH2 3 0 Na+
+
branched CgHlg CH2CH2 2 NH4 Non-limiting examples of surfactants characterized by formula (1) suitable for reducing mobility of steam are listed in Table 2.
+
R R' x v M
linear C18H37 CH2CH2CH2 0 Na+
branched C12H23 CH2CH2 2 Na+
linear C18H37 CH(CH3)CH2CH2 0 Na+
linear C18H37 CH2CH2 1 3 Na+
linear C18H37 CH2CH2 3 0 Na~
linear C18H37 CH2CH2 0 2 NH4 g 13~3~5 In selecting mobility control surfactants of this invention for a particular 100ding operation, the effect~ of gas composition should be-considered. A mobility control sy6tem comprising a surfactant represented by formula (l) above and steam will generally have higher mobility than a mobility control system comprising the same surfactant and other gases such as C02 and N2. Since the mobility of gas in this invention tends to decrease as the number of carbon atoms of the lipophile portion of the surfactant increases, the number of carbon atoms of R in formula (l) is generally higher for use in steam floods than the number of carbon atoms of R for use in other gas floods.
Referring again to formula (1), when m = 0, the R' alkyl group is absent, and the surfactant contains a sulfate group. It is well known to those skilled in the art that sulfate surfactants are susceptible to rapid chemical degradation by hydrolysis of the sulfate group at high temperature and/or low pH. The product of the degradation reaction tends to be less effective as a mobility-reducing agent, and may have significantly higher retention than the original surfactant.
For this reason, surfactants having m = 0 would generally not be used in flooding processes where the temperature is high, such as steam flooding, or where pH is low, such as C02 flooding. Surfactants having m = 0 may, however, be used under conditions where the rate of hydrolysis of the sulfate group is low. Examples of such conditions may include hydrocarbon or inert gas flooding at low temperature, or C02 flooding at low temperature in a reservoir where pH is buffered by reservoir minerals to a level at which hydrolysis ~ 8 acceptably slow.
-lo- 13137~
Particularly preferred mobility control systems of this inventian include surfactants having a composition characterized by the formula ~ --R ~ O(CH2CH20)yR'S03M (2) where: R is a C6 to C18 linear or branched alkyl chain for use in C02, inert gas, and hydrocarbon gas floods, and R is a linear or branched C12 to C30 alkyl chain for use in steam floods; y i6 0 to 6; R' is an alkyl group containing two or three carbons; and each M is an alkali metal ion.
As understood by those skilled in the art, the optimum surfactant for a particular gas flooding process will depend on the reservoir in which it is used. The optimum values of n, m, x, and y in formula (1) for a particular gas flooding operation will depend on the reservoir conditions of temperature, pressure, permeability, salinity, oil composition, and the like. The optimum surfactant maybe determined by performing core displacement tests using procedures known to those skilled in the art. Such tests may be used to select a surfactant that has low retention, can be used at low concentration, provides a substantial but not excessive reduction of gas mobility, and does not impair the recovery of the oil.
The surfactants of the present invention may be prepared by known procedures. The following is a description of one way of -ll- 1 3 ~
preparing such surfactants. For those surfactants having two or more carbon atoms attached to the benzene ring, the synthesis procedure usually begins by reacting phenol with olefins at temperatures and pressures sufficient to alkylate the phenol. The reaction is conducted in the presence of an effective amount of an acid catalyst such as boron triflouride, sulfuric acid, phosphoric acid, or sulfonic acid. The alkyl phenols may then be reacted with alkylene oxides in the presence of a base to provide alkyl-phenyl polyalkoxy alcohols.
The alkoxy derivatives may then be reacted with a sultone such as propane sultone or butane sultone to form an alkyl phenol alkoxy monosulfonate. A sulfonate group may be added on the aromatic ring to produce a disulfonate by sulfonating the alkyl phenol alkoxy monosulfonate product with a suitable sulfonating agent such as chlorosulfonic acid. The disulfonic acid may then be neutralized with a base such as 50% NaOH.
The present invention is useful where it is desirable to reduce gas mobility in an area of a subterranean, oil-containing formation to facilitate production of oil from or displacement of oil through the pores of the formation. The formation may be any light or heavy oil reservoir having a permeability suitable for an application of a fluid to displace oil away from a well borehole in a well-cleaning operation or to displace oil through the formation to a producing location in an oil recovery operation.
In general, the gaseous fluids can comprise steam, carbon dioxide, inert gases such as air and nitrogen, hydrocarbons such as methane, ethane, propane, and natural gas, and mixtures thereof.
-12~ 3~
Gas and aqueous surfactant solution may be-in~e~ted ineo the formation in the form of alternating banks. The gas and aqueous surfactant solution will mix in the format;on. However, where desirable, the gas and aqueous solution may be injected simultaneously, as a dispersion of the gas in the liquid or as a pair of co-flowing streams of the two fluids within a common conduit. The components are preferably injected at a pressure sufficient to displace the oil without fracturing the reservoir. However, in low permeability reservoirs controlled fractures of limited extent may be required to obtain adequate injectivity.
In the practice of one embodiment of this invention, C02 is injected into an oil-bearing subterranean formation through an injection well. The highly mobile gas will tend to flow preferentially through the more permeable rock sections. The C02 mobilizes the recoverable oil in those sections. Gas injection continues until sufficient gas has been injected to ensure recovery of a substantial portion of the oil in the more permeable zones, or until gas breakthrough occurs at the production well which is spaced apart from the injection well. A bank of brine containing a surfactant characterized by formula (1) above is then injected, followed by a second bank of C02. The surfactant solution will preferentially enter the more permeable zones and will reduce gas mobility in those areas, thus diverting C02 to previously unswept zones of the formation. Banks of surfactant solution may be alternated with banks of C02. Optionally, the composition of surfactant in the aqueous solution may be varied from one bank to the next to optimize the process. If desired, a bank of drive fluid may be injected after the -13- 1~13755 last C02 bank has been injected to displace the C02 through the formation. -- ~-In another embodiment of this invention, a small amount of surfactant characterized by formula (1) above is added to water duringthe last stage of a waterflood operation. Surfactant is injected before start-up of a gas injection project to avoid time delays associated with injecting an additional surfactant bank after the usual waterflood operation has been completed.
The process of this invention may be applied to a 6ubterranean, oil-containing formation penetrated by at least one injection well and at least one spaced-apart production well. The injection well is perforated or other fluid flow communication is established between the well and the formation. The production well is completed in fluid communication with a substantial portion of the vertical thickness of the formation. While recovery of the type contemplated by this invention may be carried out with only two wells, this invention is not limited to any particular number of wells. The invention may be practiced using a variety of well patterns as is well known in the art of oil recovery, such as a repeated five-spot pattern in which each injection well is surrounded with four production wells, or in a line-drive arrangement in which a series of aligned injection wells and a series of aligned production wells are utilized.
This process can also be used in "huff and puff" operations through a single well. In the huff and puff procedure, the reduced gas mobility is generated through the same well that is subsequently -14- i3137~
used for production. The reduced gas mobility improves the injection profile. The gas bility in swept zones is greatly reduced so the gas will invade the previously unswept tighter ~ones. The well may be shut in for a period of time before placing it on the production cycle. After the production cycle, additional cycles of injection and production can be utilized.
The aqueous surfactant solution used in this invention may be prepared from brine or carbonated water. Preferably the water available at the injection well site, often formation brine, will be used to prepare the aqueous surfactant solution.
The concentration of surfactant in the aqueous solution will ordinarily range from about 0.01 to 2% by weight and preferably from about 0.05 to 1%, and still more preferably from 0.05 to 0.5%.
As known to those skilled in the art, the volumes required for the banks of aqueous solution and gas are different for different reservoirs, but it can be estimated by known proccdures with reasonable accuracy. Generally, the total pore volume of surfactant solution used in this invention will range from 0.01 to l and preferably from 0.1 to 0.5 pore volume.
C2 used in this invention can be obtained from any ; 25 available source. It is not necessary that it be pure. The C02 that is produced through the production wells can be separated therefrom and reinjected into the formation. Recycling methods for C2 are generally known and do not need further explanation.
-1S- ~ 7 ~ ~
Steam used in the present invention can be generated as a dry, superheatedj or wet steam and subsequently mixed with aqueous liquid. The steam can be generated at surface or downhole locations and mixed with the aqueous surfactant solution at surface or downhole locations. Optionally, the steam may include a gas that is noncondensable at reservoir temperature and pressure.
Experimental Results This invention is further illustrated by the following laboratory experiments, which demonstrate the operability of the invention. The experiments are not intended as limiting the scope of the invention as defined in the appended claims.
All of the core flooding laboratory experiments described below used 1 in. X 1 in. X 12 in. (2.54cm X 2.54cm X 30.5cm) Berea sandstone cores. Differential pressures were monitored between inlet and outlet and between three pairs of taps 1 in. (2.54 cm) apart located 2 in. (5.04 cm), 6 in. (15.24 cm) and 10 in. (25.40 cm) from the inlet. All experiments were carried out at 2000 psi (13,789 kPa) with decane as the oil phase. Two high-salinity brines were used:
; 3.5% and 7.0% by weight total dissolved solids (TDS). Both brines had high contents of divalent ions, with a weight-ratio of CaC12 to NaCl of 1 to 4. Two temperatures were used: 100F (37.8C) and 150F
(65.6C). Five corefloods are discu66ed below in detail. All of the cores were flooded with oil (decane) to connate water saturation and then waterflooded with brine at a rate of 3 ft/day (0.91 m/day) prior to carrying out the experiments. Decane was completely miscible with -16- 1~13~
C2 at the conditions o the tests. The injection rate~of C~2-through the cores was 1 ft/day (0.30 m/day) and the injection rate of surfactant solution was 3 ft/day (0.91 m/day). At this rate, no oil was produced when only surfactant solution flowed through the cores.
Table 3 below sets forth core permeability, brine concentration, temperature, and injection sequence for each run.
Berea Core Permea- Brine, Temp., Run bility TDS C Iniection Sequence 1 450 md 3.5% 37.8 C2 Flood 2 550 md 3.5~ 37.8 0.1~ Surfactant, then 3 530 md 7.0~ 37.8 0.1% Surfactant, then 4 650 md 3.5% 65.6 0.1~ Surfactant, then 520 md 3.52 37.8 0.5% Surfactant, then The surfactant in runs 2-5 was a linear C16 alkyl phenol disulfonate (C16APDS), a surfactant represented by formula (1) above where x = 0, y = 0, and m = 3.
The active surfactant contained 92% disulfonate and 8%
monosulfonate. The monosulfonate component had the sulfonate group on the aromatic ring.
-17- 1313~
The objectives of the tests were to reduce C0z mobility in a core containing waterflood residual oil- and displace the residual oil with the C02. In all of the core floods in which surfactant was injected, C02 mobility was reduced by an unsteady-state process -involving a two step injection sequence: injection of surfactantsolution followed by injection of C02. In runs 2-5, sufficient surfactant solution was injected so that the effluent surfactant concentration nearly reached the influent surfactant concentration prior to injection of C02.
The comparative mobility, oil recovery and surfactant retention of each run are summarized in Table 4 below. The comparative mobility i8 defined as the ratio of the mobility of the gas-aqueous surfactant solution mixture to water mobility at residual oil saturation. At 2.0 pore volumes of C02 injection, the mobility of the aqueous phase is extremely low, so that for good approximation the comparative mobility is simply the mobility of C02. A
comparative mobility greater than unity indicates the gas will be more mobile than water at residual oil saturation. Generally, for effective mobility control in C02 floods, the comparative mobility should be below about 1, depending on field conditions. A comparative mobility above about 1 would not be desirable due to instability at the displacement front resulting in fingering, bypassing and low displacement efficiency. However, any reduction of mobility brought about by the injection of surfactant solution of this invention will be beneficial, even if the comparative mobility somewhat exeeds 1.
-18- 13137~S
. .
RUN OIL SAlVRA- SURFACTANT OIL COMPARA--TION BEFORE RETENTION RECOVERY TIVE
SURFACTANT at 1.2 M08ILIl~Y
INJECTION PV C02 at 2.0 PV
TION JECTION
mg/g rock ~ Sor .
1 0.34 _ 80 2 0.440.18 76 0.2 3 0.420.22 82 0.4 4 0.490.17 85 0.3 0.490.20 80 0.25 C2 Flood (No Surfactant) - Run 1 Run 1 provided a base case for the other runs. The comparative mobility of C02 characteristically increased to 10 after C2 breakthrough. The high mobility i8 related to the low viscosity of CO2, about 0.06 cp at 2000 psi (13,789 kPa) and 100F (37.8C).
The oil recovery was about 80% of waterflood residual oil saturation (Sor) after 1.2 pore volumes of C02 were injected.
Mobility Control Process in Waterflooded Core - Run 2 `:
An aqueous solution containing 3.5% total dissolved solids and 0.1% C16APDS was injected into a waterflooded core. No additional oil was removed from the core during injection of over 3 pore volumes of the surfactant solution. During the subsequent CO2 injection, CO2 mobility was much lower than in Run 1. As shown in FIGURE l, the comparative mobility dropped gradually, leveling off at about 0.2 after 2PV of CO2 injection.
~ 3 ~
--lg--The oil recovery at-1.2 pore volumes of C02 injected was 76Z of waterflood residual oil ~S ~, similar to that o~tained in Run 1.
Effect of Salinity, Temperature and Surfactant concentration - Runs 3, 4, and 5 Runs 3, 4, and 5 were similar to Run 2 except that the brine was more saline in Run 3, the temperature was higher in Run 4, and the surfactant concentration was greater in Run 5.
Despite the large changes in conditions, neither surfactant retention, oil recovery, nor comparative mobility was significantly different from the values obtained in Run 2, as shown in Table 4.
These results suggest that the performance of a gas mobility control process using the surfactants of this invention is relatively insensitive to reasonable variations in salinity, temperature, and surfactant concentration.
The principle of the invention and the best mode contemplated for applying that principle have been described. It will be apparent to those skilled in the art that various changes ~ay be made to the embodiments described above without departing from the spirit and scope of this invention as defined in the following claims. It is, therefore, to be understood that this invention is not limited to the specific details shown and described.
Claims (26)
1. A method for recovering oil from a subterranean oil-containing formation comprising injecting into the formation a gas selected from the group consisting of carbon dioxide, hydrocarbon gas, inert gas, and steam, and injecting into the formation an agueous solution containing a surfactant characterized by the formula where R is a linear or branched chain alkyl group with n carbon atoms wherein n ranges from 0 to about 18, except that if the gas is steam n ranges from about 9 to about 30;
x ranges from 0 to about 20 and y ranges from 0 to about 20, provided x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 0 to 4, except that if the gas is steam m ranges from 1 to 4, with the proviso that the sum of v + y + m is at least one; and each M+ is a cation.
x ranges from 0 to about 20 and y ranges from 0 to about 20, provided x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 0 to 4, except that if the gas is steam m ranges from 1 to 4, with the proviso that the sum of v + y + m is at least one; and each M+ is a cation.
2. The method of claim 1 wherein the gas is selected from the group consisting of carbon dioxide, air, nitrogen, methane, ethane, propane, and natural gas or mixtures thereof.
3. The method of claim 2 wherein R is a C6 to C18 linear or branched alkyl chain, x is 0, y ranges from 0 to 6, R' is an alkyl group containing two or three carbon atoms and each M+ is an alkali metal ion.
4. The method of claim 2 wherein R is C16H33 linear alkyl chain, x is 0, y is 0, R' is CH2CH2CH2 and each M+ is Na+.
5. The method of claim 1 wherein the gas is steam.
6. The method of claim 5 wherein R is a linear or branched C12 to C30 alkyl chain, x is 0, y ranges from 0 to 6, R' is an alkyl group containing two or three carbon atoms and each M is an alkali metal ion.
7. The method of claim 5 wherein R is linear C18H37, x is 0, y is 0, R' is CH2CH2CH2, and each M+ is Na+.
8. The method of claim 5 wherein R is branched C12H23, x is 0, y is 2, R' is CH2CH2, and each M+ is Na+.
9. The method of claim 1 wherein the subterranean oil-containing formation is penetrated by a well further comprising injecting the aqueous solution containing said surfactant into the formation though said well, injecting gas into the formation through said well, and recovering oil from said well.
10. The method of claim 1 wherein the surfactant concentration in the aqueous solution is 0.01 to 2% by weight.
11. The method of claim 1 wherein the subterranean oil-containing formation is penetrated by at least one injection well and at least one spaced-apart production well further comprising injecting the aqueous solution containing said surfactant into the formation through the injection well, injecting the gas into the formation through the injection well, and recovering oil from the production well.
12. The method of claim 1 wherein said steps of injecting said gas and injecting said aqueous solution containing said surfactant are performed sequentially.
13. The method of claim 1 wherein said steps of injecting said gas and injecting said aqueous solution containing said surfactant are performed simultaneously.
14. A process for recovering oil from a porous, oil-containing subterranean formation penetrated by an injection well and a spaced apart production well, which comprises injecting through said injection well and into said formation an aqueous solution containing a surfactant characterized by the formula where R is a linear or branched chain alkyl group with n carbon atoms wherein n ranges from 0 to about 18;
x ranges from 0 to about 20 and y ranges from 0 to about 20, provided x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 0 to 4, with the proviso that the sum of x + y + m is at least one; and each M is a cation;
injecting CO2 through said injection well and into said formation; and producing oil from the production well.
x ranges from 0 to about 20 and y ranges from 0 to about 20, provided x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 0 to 4, with the proviso that the sum of x + y + m is at least one; and each M is a cation;
injecting CO2 through said injection well and into said formation; and producing oil from the production well.
15. The process of claim 14 wherein the surfactant is characterized by the formula where R is C6 to C18 linear or branched alkyl chain, y ranges from 0 to 6, R' is an alkyl group containing two or three carbon atoms, and each M+ is an alkali metal.
16. The process of claim 14 wherein R is C16H33 linear alkyl chain, x is 0, y is 0, R' is CH2CH2CH2 and each M+ is Na+.
17. The process of claim 14 wherein R is branched C9H19, x is 0, y is 2, R' is CH2CH2 and each M+ is Na+.
18. A process for recovering oil from a porous, oil-containing subterranean formation penetrated by an injection well and a spaced apart production well, which comprises injecting through said injection well and into said formation an aqueous solution containing a surfactant characterized by the formula where R is a linear or branched chain alkyl group with n carbon atoms wherein n ranges from about 9 to about 30;
x ranges from 0 to about 20 and y ranges from 0 to about 20, provided x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 1 to 4, with the proviso that the sum of x + y + m is at least one; and each M+ is a cation;
injecting steam through said injection well and into said formation; and producing oil from the production well.
x ranges from 0 to about 20 and y ranges from 0 to about 20, provided x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 1 to 4, with the proviso that the sum of x + y + m is at least one; and each M+ is a cation;
injecting steam through said injection well and into said formation; and producing oil from the production well.
19. The process of claim 18 wherein R is a linear or branched C12 to C30 alkyl chain, x is 0, y ranges from 0 to 6, R' is an alkyl group containing two or three carbon atoms and each M+
is an alkali metal ion.
is an alkali metal ion.
20. The process of claim 18 wherein R is linear C18H37, x is 0, y is 0, R' is CH2CH2CH2, and each M+ is Na+.
21. A method for reducing gas mobility in a subterranean oil-containing formation having regions of varying permeability comprising injecting into the formation a gas selected from the group consisting of carbon dioxide, hydrocarbon gas, inert gas, and steam, and injecting an aqueous solution containing a surfactant characterized by the formula where R is a linear or branched chain alkyl group with n carbon atoms wherein n ranges from 0 to about 18, except that if the gas is steam n ranges from about 9 to about 30;
x ranges from 0 to about 20 and y ranges from 0 to about 20, with the proviso that x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 0 to 4, except that if the gas is steam m ranges from 1 to 4, with the proviso that the sum of x + y + m is at least one; and each M+ is a cation;
whereby said gas and said aqueous solution containing said surfactant form a mixture in the formation which significantly reduces gas mobility in the more permeable regions of said formation.
x ranges from 0 to about 20 and y ranges from 0 to about 20, with the proviso that x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 0 to 4, except that if the gas is steam m ranges from 1 to 4, with the proviso that the sum of x + y + m is at least one; and each M+ is a cation;
whereby said gas and said aqueous solution containing said surfactant form a mixture in the formation which significantly reduces gas mobility in the more permeable regions of said formation.
22. A formulation useful in the displacement of oil within a porous, subterranean, oil-containing formation consisting essentially of water, gas, and a surfactant wherein the surfactant is characterized by the formula where R is a linear or branched chain alkyl group with n carbon atoms wherein n ranges from 0 to about 18, except that if the gas is steam n ranges from about g to about 30;
x ranges from 0 to about 20 and y ranges from 0 to about 20, provided x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 0 to 4, except that if the gas is steam m ranges from 1 to 4, with the proviso that the sum of x + y + m is at least one; and each M+ is a cation.
x ranges from 0 to about 20 and y ranges from 0 to about 20, provided x + y does not exceed about 20;
R' is a linear or branched chain alkyl group with m carbon atoms wherein m ranges from 0 to 4, except that if the gas is steam m ranges from 1 to 4, with the proviso that the sum of x + y + m is at least one; and each M+ is a cation.
23. The formulation of claim 22 wherein the gas is CO2.
24. The formulation of claim 23 wherein R is a C6 to C18 linear or branched alkyl chain, x is 0, y ranges from 0 to 6, R' is an alkyl group containing two or three carbon atoms and each M+ is an alkali metal ion.
25. The formulation of claim 22 wherein the gas is steam.
26. The formulation of claim 25 wherein R is a linear or branched C12 to C30 alkyl chain, x is 0, y ranges from 0 to 6, R' is an alkyl group containing two or three carbon atoms and each M+
is an alkali metal ion.
is an alkali metal ion.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US10938587A | 1987-10-15 | 1987-10-15 | |
| US109,385 | 1987-10-15 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1313755C true CA1313755C (en) | 1993-02-23 |
Family
ID=22327384
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000579493A Expired - Fee Related CA1313755C (en) | 1987-10-15 | 1988-10-06 | Oil recovery process using alkyl hydroxyaromatic dianionic surfactants as mobility control agents |
Country Status (3)
| Country | Link |
|---|---|
| CA (1) | CA1313755C (en) |
| GB (1) | GB2211224B (en) |
| NO (1) | NO884411L (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10214683B2 (en) | 2015-01-13 | 2019-02-26 | Bp Corporation North America Inc | Systems and methods for producing hydrocarbons from hydrocarbon bearing rock via combined treatment of the rock and subsequent waterflooding |
-
1988
- 1988-10-05 NO NO88884411A patent/NO884411L/en unknown
- 1988-10-06 CA CA000579493A patent/CA1313755C/en not_active Expired - Fee Related
- 1988-10-14 GB GB8824112A patent/GB2211224B/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10214683B2 (en) | 2015-01-13 | 2019-02-26 | Bp Corporation North America Inc | Systems and methods for producing hydrocarbons from hydrocarbon bearing rock via combined treatment of the rock and subsequent waterflooding |
Also Published As
| Publication number | Publication date |
|---|---|
| GB8824112D0 (en) | 1988-11-23 |
| NO884411L (en) | 1989-04-17 |
| GB2211224B (en) | 1991-12-18 |
| NO884411D0 (en) | 1988-10-05 |
| GB2211224A (en) | 1989-06-28 |
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