Micellar slug for oil recovery

BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention relates to a micellar slug suitable for use in a micellar drive for recovering oil from subterranean reservoirs. More specifically, it relates to a micellar slug capable of forming micro-emulsions having a small interfacial tension at a high salt concentration and of recovering oil at a high oil recovery efficiency from subterranean reservoirs.
2. Description of the Prior Art
It is well-known in the art that the so-called "primary recovery" methods, including pumping methods, can recover only a portion of the petroleum or crude oil (referred to as "oil" hereinafter) from subterranean reservoirs and leave substantial amounts of oil in the subterranean reservoirs.
In order to recover the remaining large amounts of oil from the subterranean reservoirs, the so-called "secondary recovery" methods have been proposed, wherein, for example, water or gas is injected into the subterranean reservoirs from an injection well at a pressure sufficient to increase the flowability of oil, steam is injected into subterranean reservoirs so as to effect the displacement of oil toward a production well, or oil in subterranean reservoirs is partially burned to heat the subterranean reservoirs so as to decrease the viscosity of the oil and increase the flowability of the oil.
Furthermore, the so-called various "tertiary recovery" methods, including a combination of secondary recovery methods and improved secondary recovery methods, have been proposed, wherein surfactants or water-soluble polymers are utilized. These methods are generally called "enhanced oil recovery" (EOR) methods.
Among the surfactants EOR methods, the recent "micellar drive" methods are to be noted. According to these methods, a micellar slug, that is, a clear micro-emulsion derived from water and oil such as petroleum, petroleum distillates, or fuel oil, is injected under pressure into the subterranean reservoirs for the recovery of oil in the subterranean reservoirs. These EOR methods are disclosed in, for example, U.S. Pat. Nos. 3,506,070, 3,613,786, 3,740,343, 3,983,940, 3,990,515, 4,017,405, and 4,059,154. These prior arts disclose that various kinds of surfactants including anionic-, nonionic-, and cationic-type surfactants can be used alone or in any mixture thereof in the formation of micellar slugs. Examples of such surfactants are petroleum sulfonates, alkylaryl sulfonates, dialkyl sulfosuccinates, alkane sulfonates, polyoxyethylene alkylether sulfates, alpha-olefin sulfonate, polyoxyethylene alkylethers, polyoxyethylene alkylphenylethers, polyol fatty acid esters, alkyltrimethyl ammonium salts, and dialkyldimethyl ammonium salts.
The micellar slugs should have the following characteristics to recover oil from subterranean reservoirs at a high efficiency:
Sufficiently low interfacial tensions between oil and the micro-emulsions and between formation water and the micro-emulsions; the same or slightly higher viscosity of the micro-emulsions than that of the oil contained in the subterranean reservoirs; and sufficient salinity tolerance of the micellar slugs a at a wide salt concentration since the salt concentration range of water contained in the subterranean reservoirs extends widely from a low to high concentration.
SUMMARY OF THE INVENTION
The object of the present invention is to provide, for the recovery of oil, a micellar slug having an excellent oil-micro-emulsion and water-micro-emulsion interfacial tensions decreasing capabilities and an excellent salinity tolerance at a wide salt concentration range and being capable of readily adjusting the viscosity thereof.
Other objects and advantages of the present invention will be apparent from the following description.
In accordance with the present invention, there is provided a micellar slug, for the recovery of oil, consisting essentially of a hydrocarbon, an aqueous medium, a surfactant, and a cosurfactant, the surfactant containing, as an essential component, an internal olefin sulfonate having 10 to 26 carbon atoms, a hydroxyalkane sulfonate content of not less than about 40% by weight and a disulfonate content of not more than 20% by weight. The internal olefin sulfonates are derived from the sulfonation of an internal olefin having the general formula:
R-CH.dbd.CH-R'
wherein R is a straight- or branched-chain alkyl group having 4 to 23 carbon atoms, R' is a straight- or branched-chain alkyl group having 1 to 12 carbon atoms provided that the total carbon atom numbers of R and R' is 8 to 24 and 50% by weight or more of the internal olefins is that having R' with 1 to 4 carbon atoms.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
The micellar slugs desirably used for the recovery of oil are transparent or translucent micro-emulsions containing about 2% to about 90% by weight of a hydrocarbon, about 4% to about 95% by weight of an aqueous medium, about 1% to about 30% by weight of a surfactant containing, as an essential constituent, an internal olefin sulfonate having 10 to 26 carbon atoms, and about 0.1% to about 20% by weight of a cosurfactant.
The aqueous medium usable in the formation of the micellar slug of the present invention includes soft water and brine. For example, rain water, river water, lake water, subterranean water, oil stratum water, and seawater can be freely used in the formation of the micellar slug of the present invention.
Internal olefin sulfonates having a good salinity tolerance and hard-water resistance are used as an essential component of the surfactant in the micellar slugs of the present invention. Therefore, brine having a salt concentration of up to about 10% by weight can be used in the formation of the micellar slugs of the present invention. When another adequate surfactant is used together with the internal olefin sulfonate or when a certain cosurfactant is selected, brine including up to about 15% by weight of inorganic salts can be used in the formation of the micellar slugs of the present invention. Furthermore, the micellar slugs of the present invention can be resistant against multivalent metal ions, for example, about 5,000 ppm of a Mg ion (i.e., about 2.6% by weight of MgSo.sub.4) Thus, water (or brine) usable in the formation of the micellar slugs of the present invention can contain 0% to about 15% by weight, desirably about 0.5% to about 12% by weight and more desirably about 1% to about 10% by weight, of inorganic salts. Typical examples of the inorganic salts contained in the water (or brine) are NaCl, KCl, Na.sub.2 SO.sub.4, and K.sub.2 SO.sub.4. For instance, seawater contains about 3.5% by weight of inorganic salts including about 1,600 ppm, in terms of a Mg ion, of divalent metal ions. This salt concentration is within the desirable salt concentration range of the present invention.
The internal olefin sulfonates usable as an essential surfactant in the present invention are those obtained by sulfonating internal olefins containing as a main constituent vinylene-type monoolefin having a general formula:
R-CH.dbd.CH-R'
wherein R is a straight- or branched-chain alkyl group having 4 to 23 carbon atoms, R' is a straight- or branched-chain alkyl group having 1 to 12 carbon atoms, provided that the total carbon atom numbers of R and R' is 8 to 24, desirably 10 to 22 and 50% by weight or more of the internal olefins is that having R' with 1 to 4 carbon atoms and optionally containing about 33% by weight (about one third of the olefins) or less of tri-substituted type monoolefins, followed by neutralizing the sulfonated products with appropriate bases and, then, optionally, hydrolyzing the neutralized products. The internal olefin sulfonates thus prepared generally contain about 10% to about 60% by weight of alkenyl sulfonates having a double bond and about 90% to about 40% by weight of hydroxyalkane sulfonates and also contain about 80% by weight or more of monosulfonates and about 20% by weight or less of disulfonates. It should be noted, however, that internal olefin sulfonates having the compositions different from the above-mentioned composition ratios can be prepared by appropriately selecting the sulfonation conditions and hydrolysis conditions. Generally speaking, the increase in the carbon atom number of the internal olefin tends to result in an increase in the composition ratio of the alkenylsulfonate. On the other hand, the increase in the mol ratio of the sulfonating agent to the internal olefin during the sulfonation tends to result in an increase in the composition ratio of the disulfonate.
The internal olefin sulfonates usable in the present invention should have both a long chain aliphatic group and a short chain aliphatic group in the lipophilic group. When no short chain aliphatic group is present in the internal olefin sulfonates (i.e., in the case of alpha-olefin sulfonates), the viscosity of the micro-emulsions is high and, therefore, the decrease in the viscosity is difficult while the low interfacial tension and the stability of the micro-emulsions are maintained. On the other hand, when both aliphatic groups are long chain groups, the salinity tolerance is undesirably decreased whereby the micellar slugs cannot be applied to the subterranean reservoirs having a high salt concentration. For this reason, the internal olefin sulfonates having C.sub.1 to C4 alkyl group, desirably C.sub.1 to C4 linear alkyl group, as R' in the above-mentioned general formula, snould be 50% by weight or more, desirably 60% by weight or more. The desirable alkyl group R in the above-mentioned general formula is a straight-chain alkyl group. Furthermore, the disulfonate content in the internal olefin sulfonates should be about 20% by weight or less, desirably about 15% by weight or less. The hydroxyalkane sulfonate content in the internal olefin sulfonates should be about 40% by weight or less, desirably about 45% to about 90% by weight.
The internal olefin sulfonates usable in the present invention can be alkali metal salts, alkaline earth metal salts, ammonium salts, and organic amine salts thereof. The desirable counter cations are Na, K, Mg, Ca, NH.sub.4, and alkanolammonium.
Examples of internal olefin sulfonates usable in the formation of the micellar slugs of the present invention are: internal olefin sulfonate having 12, 13, 14, 15, 16, 18, 20, 22, 24, 12-13, 12-16, 13-14, 14-16, 14-18, 15-17, 16-18, 16-20, 18-20, 18-24, and 20-24 carbon atoms. These sulfonates may be used alone or in any mixture thereof.
As mentioned above, the micellar slugs of the present invention contain about 1% to about 30% by weight of the surfactant. However, the micellar slugs desirably contain about 3% to about 25% by weight of the surfactant, taking into consideration both low interfacial tensions and reasonable cost. The amount of the higher internal olefin sulfonates having 10 to 26 carbon atoms should be at least 50% by weight, desirably 60% by weight or more, based on the total amount of the surfactants contained in the micellar slugs.
The hydrocarbons usable as an oil component in the present invention include, for example, petroleum, liquefied petroleum gas, crude gasoline (naphtha), kerosine, diesel oil, and fuel oil. The recovered petroleum is desirably used due to its low cost and availability as well as its composition, which is similar to that of the oil contained in subterranean reservoirs. As mentioned above, the micellar slugs of the present invention can contain about 2% to about 90% by weight of hydrocarbons. The desirable concentration of hydrocarbons is within the range of about 3% to about 40% by weight whereby an oil-in-water (O/W) type emulsion is formed, since the use of a large amount of hydrocarbons is not economical.
The cosurfactants used in the formation of the micellar slugs of the present invention are an essential constituent for forming micro-emulsions associated with the surfactants. The cosurfactants usable in the present invention are those having an alcoholic hydroxyl group. The desirable cosurfactants are alcohols having the general formula:
R"O(CH.sub.2 CH.sub.2 O).sub.n H
wherein n is a number of from 0 to about 4 and R" is an alkyl or alkenyl group having 4 to 8 carbon atoms when n is zero and an alkyl or alkenyl group having 6 to 15 carbon atoms, a phenyl group, or an alkylphenyl group having 7 to 16 carbon atoms when n is not zero. The aliphatic groups of R" may be straight-chain or branched-chain groups.
Examples of such alcohols are butanols, pentanols, hexanols, 2-ethylhexanol or other octanols, polyoxyethylene hexylethers (n=1), polyoxyethylene decylethers (n=2), polyoxyethylene tridecylethers (n=4), polyoxyethylene butylphenylethers (n=2), polyoxyethylene nonylphenylethers (n=3), and polyoxyethylene dodecylphenylethers (n=4).
As mentioned above, the micellar slugs of the present invention can contain about 0.1% to about 20% by weight of the cosurfactants. However, the desirable concentration of the cosurfactants is within the range of about 1% to about 10% by weight from the viewpoints of the stability of the micro-emulsions and the decreasing capability for interfacial tension between oil and water.
As mentioned above, the micellar slugs of the present invention contain internal olefin sulfonates having 10 to 26 carbon atoms as an essential or major constituent of the surfactants. However, other auxiliary surfactants can also be included, together with the internal olefin sulfonates, taking into consideration the desired interfacial tension between oil and water, the desired viscosity, the adsorbability of the surfactants to rocks constituting the subterranean reservoirs, and the cost and availability of the surfactants.
Examples of such auxiliary surfactants are anionic surfactants and nonionic surfactants such as petroleum sulfonates, alkylbenzene sulfonates, polyoxyethylene alkylether sulfates, dialkyl sulfosuccinates, alpha-olefin sulfonates, paraffin sulfonates, soaps, higher alcohol ethoxylates, alkylphenol ethoxylates, polyol fatty acid esters, fatty acid alkylol amides, and polyoxyethylene fatty acid amides.
The viscosity of the micellar slugs of the present invention can be suitably adjusted by selecting the kinds and amounts of the constituents of the micro-emulsions. However, when a micellar slug having a high viscosity is desired, an appropriate known thickening agent such as a water-soluble polymer can be added to the micellar slugs. Examples of thickening agents usable in the formation of the micellar slugs are heteropolysaccharides produced by microbes, napthalenesulfonic acid-formaldehyde condensates, polyacrylamides, polyacrylates, hydroxyethylcelluloses, and carboxymethylcelluloses.
The micellar slugs of the present invention can be readily obtained by any known method of production. For example, the hydrocarbons, the surfactants, the aqueous medium, and the cosurfactants can be mixed in any mixing order by using conventional mixing devices, mixing temperatures, and mixing pressures.
The recovery of oil from subterranean reservoirs can be carried out by means of any conventional micellar drive method by using the micellar slugs of the present invention. For instance, the micellar slugs are injected under pressure into at least one injection well of the subterranean reservoirs. Then, at least one driving fluid such as flood water and/or aqueous solution of the above-mentioned thickening agent is injected into the injection well so as to transfer or drive the remaining oil toward an oil production well and to recover the oil from the production well. The suitable amount of the micellar slugs injected into the injection well is about 5% to about 25% by volume of the porosity of the subterranean reservoirs.
The suitable salt concentration of the subterranean water in the subterranean reservoirs where the micellar slugs of the present invention can be applied is 0% to about 15% by weight, desirably about 0.1% to about 12% by weight and, more desirably, about 0.5% to about 10% by weight. The salt concentration of water used in the formation of the micellar slugs is desirably the same as that of the subterranean water from the viewpoints that the salt concentration is changed during the sweeping although this is not essential.
As mentioned hereinabove, since the micellar slugs of the present invention contain the internal olefin sulfonates having a liphophilic group with both long and short chain aliphatic groups as a surfactant. The resultant micellar slugs therefore have an excellent salinity tolerance and hard-water resistance and are capable of forming micro-emulsions at a very wide salt concentration from soft water to brine having a high salt concentration. Furthermore, the micellar slugs of the present invention have very small interfacial tensions between water and the micro-emulsions and between oil and the micro-emulsions. The viscosity of the micro-emulsions formed from the present micellar slugs is low and can be optionally adjusted by the use of a thickening agent. As a result, the following remarkable advantageous features can be obtained:
(1) Either soft water, seawater, or subterranean water having a high salt concentration can be freely used;
(2) The micellar slugs injected into the subterranean reservoirs are subjected to no substantial adverse affects by inorganic salts present in the subterranean reservoirs;
(3) The micellar drive method can be readily applied in subterranean reservoirs containing oil having a low viscosity to a high viscosity; and
(4) A high oil recovery efficiency can be attained since the micro-emulsions are not destroyed by oils and water contained in the subterranean reservoirs.

EXAMPLES
The present invention now will be further illustrated by, but is by no means limited to, the following examples, in which the component ratios or amounts of samples used are based on "% by weight" unless otherwise specified.
EXAMPLE 1
Micro-emulsions were prepared by weighing 10.5% of sodium C.sub.15 -C.sub.17 internal olefin sulfonates (C.sub.15 -C.sub.17 IOS-Na) containing various hydroxyalkane sulfonate contents as a surfactant, 4.5% of amyl alcohol as a cosurfactant, 17% of fuel oil (ASTM No. 2 oil), and 68% of an aqueous solution of 3% or 5% of sodium chloride dissolved in demineralized water as brine in a beaker. The resultant mixture was stirred at 100 rpm for 30 minutes at a temperature of 71.degree. C.
The internal olefin sulfonates used as a surfactant were prepared by isomerizing C.sub.15 -C.sub.17 alpha-olefins to internal olefins in the presence of an acid catalyst, followed by the sulfonation. About 80% of the double bond in the internal olefins after isomerization was present at the C.sub.2 -C.sub.5 positions. The internal olefin sulfonates having different hydroxyalkane sulfonate contents were prepared by changing the mole ratio of the internal olefins and SO.sub.3 in the sulfonation reaction. The internal olefin sulfonate sample containing 90% of hydroxyalkane sulfonate was prepared by extracting sultone from the sulfonated slurry by hexane, followed by the hydrolysis in toluene. The internal olefin sulfonate sample containing 30% of hydroxyalkane sulfonate was prepared by neutralizing the above-mentioned hexane extract residue, followed by adjusting the given content.
The micro-emulsion forming capabilities, the interfacial tension decreasing capabilities, and the oil recovery efficiencies of the micro-emulsions thus prepared were evaluated as follows. The results are shown in Table 1.
The micro-emulsion forming capabilities were determined from the visual appearances of the micro-emulsions according to the following:
o . . . A transparent or translucent and homogeneous micro-emulsion was formed
x . . . An opaque suspension, rather than a micro-emulsion was formed.
The interfacial tensions were measured by a spinning drop type tensionmeter at 71.degree. C. in an appropriately diluted system.
The oil recovery tests were carried out by using Berea sandstone core having a size of 3.8 cm diameter and 28 cm length and having a permeability of about 500 mD and a porosity of about 20%. The core sufficiently saturated with brine was set in a core holder and, then, fuel oil was injected under pressure into the core at a feed rate of 6 cc/min until no brine was discharged. Then, brine was injected under pressure at the same feed rate in a water drive method until the content of the fuel oil in the effluent became less than 0.1%. Thus, the fuel oil was recovered. After the water drive method the core holder and the micro-emulsions were placed in a constant temperature bath at a temperature of 71.degree. C. for a micellar drive method. The micro-emulsions were first injected under pressure into the cores in an amount of 10% by volume of the pore volume, a polymer solution (i.e., 1000 ppm of Xanthan gum solution in a brine solution) was then injected under pressure in an amount of 100% by volume of the pore volume, and, finally, a brine was injected under pressure in an amount of 100% by volume of the pore volume. Thus, the fuel oil was recovered. The injection rate under pressure was 2 feet/day. The oil recovery efficiency was determined by measuring the amount of water in the core after the test in a toluene azeotropic method to convert the recovery amount of the fuel oil.
TABLE 1______________________________________Sample No. 1 2 3 4 5 6______________________________________Surfactant C.sub.15 -C.sub.17 IOS--NaHydroxyalkane sulfonate 30 70 90content (%)Disulfonate content 10 8 8(% per effective component)NaCl content in 3 8 3 8 3 8brine (%)Micro-emulsion forming o x o o o ocapabilityInterfacial tension 5.3 -- 5.8 4.8 6.1 5.1(.times. 10.sup.-3 dyne/cm)Oil recovery (%) 91 -- 90 92 90 91______________________________________
In Table 1, sample Nos. 3 to 6 are examples according to the present invention. Sample No. 1 illustrates that micro-emulsions is formed at a low salt concentration when the hydroxyalkane sulfonate content is less than 40%. Sample No. 2 illustrates that the salinity tolerance becomes worse when the hydroxyalkane sulfonate content is less than 40%.
EXAMPLE 2
Micro-emulsions were prepared by weighing 10.5% of C.sub.16 -C.sub.18 IOS-Na containing 70% of hydroxyalkane sulfonate, 8%, based on the effective component, of disulfonate as a surfactant, 4.5% of amyl alcohol as a cosurfactant, 17% of fuel oil (ASTM No. 2 oil) as a hydrocarbon, and 68% of seawater or an aqueous solution of a given amount of sodium chloride, magnesium or calcium chloride dissolved in demineralized water as brine in a beaker. The resultant mixture was stirred at 100 rpm for 30 minutes at a temperature of 71.degree. C. The C.sub.16 -C.sub.18 IOS-Na used above was prepared by sulfonating internal olefin containing about 75% of the double bonds at the C.sub.2 -C.sub.5 positions.
The micro-emulsion forming capabilities, the interfacial tensions, and the oil recovery efficiencies of the micro-emulsions were evaluated in the same manner as in Example 1. The results are shown in Table 2 below.
TABLE 2______________________________________Sample No. 7 8 9 10 11 12______________________________________Surfactant C.sub.16 -C.sub.18 IOS--NaBrine NaCl seawater 1 5 7 7 12(%) CaCl.sub.2 -- -- 0.7 -- -- MgCl.sub.2 -- -- -- 0.7 --Micro-emulsion o o o o o oforming capabilityInterfacial tension 5.1 7.1 5.4 4.9 4.8 4.3(.times. 10.sup.-3 dyne/cm)Oil recovery (%) 91 89 91 91 92 92______________________________________
EXAMPLE 3
Internal olefin sulfonates used as a surfactant were prepared by internal olefins obtained from C.sub.16 alpha-olefin in different isomerization conditions (i.e., catalyst amounts and reaction times). The positions of the double bonds of the isomerized C.sub.6 internal olefins are shown in Table 3.
TABLE 3______________________________________ Sample No.Double bond position 13 14______________________________________ C.sub.1 -- --C.sub.2 26 4C.sub.3 35 12C.sub.4 21 24.sup. C.sub.5-6 10 27.sup. C.sub.7-8 8 33______________________________________ (% by weight)
Micro-emulsions were prepared by weighing 10.5% of C.sub.16 IOS-Na samples 13 and 14 obtained above as a surfactant, 4.5% of amyl alcohol as a cosurfactant, of fuel oil (ASTM No. 2 oil) as a hydrocarbon, and 68% of an aqueous solution of 8% of sodium chloride dissolved in demineralized water as brine in a beaker. The resultant mixture was stirred at 100 rpm for 30 minutes at a temperature of 71.degree. C.
The oil recovery tests were carried out by using these samples in the same manner as described in Example 1. As a result, the oil recovery efficiency of the micro-emulsion derived from the sulfonation product of internal olefin sample No. 13 was 93% and that of sample No. 14 was 90%. This difference in the oil recovery efficiency due to the difference in the double bond positions of the starting internal olefin is not very large. However, this difference of the oil recovery efficiency cannot be neglected when the micellar slugs are applied to the subterranean reservoirs. Thus, the starting internal olefin containing a larger amount of the double bonds at the C.sub.2 -C.sub.5 position is desirable in the practice of the present invention.
EXAMPLE 4
Micro-emulsions were Prepared by weighing 10.5% of C.sub.13 -C.sub.14 IOS-Mg, C.sub.14 -C.sub.18 IOS-Na or C.sub.18 -C.sub.20 IOS-K as a surfactant, 4.5% of amyl alcohol as a cosurfactant, 17% of fuel oil (ASTM No. 2 oil) as a hydrocarbon, 68% of an aqueous solution of 8% of sodium chloride dissolved in demineralized water as brine in a beaker. The resultant mixture was stirred at 100 rpm for 30 minutes at a temperature of 71.degree. C.
The micro-emulsion forming capabilities, the interfacial tensions, and the oil recovery efficiencies of the micro-emulsions were evaluated in the same manner as in Example 1. The results are shown in Table 4 below.
TABLE 4__________________________________________________________________________Sample No. 15 16 17__________________________________________________________________________Surfactant C.sub.13 -C.sub.14 IOS--Mg C.sub.14 -C.sub.18 IOS--Na C.sub.18 -C.sub.20 IOS--KDouble bond position 88 79 70(C.sub.2 -C.sub.5) (%)*Hydroxyalkane sul- 72 70 75fonate content (%)Disulfonate content 7 7 9(% per effectivecomponent)Micro-emulsion o o oforming capabilityInterfacial tension 9.1 4.7 4.3(.times. 10.sup.-3 dyne/cm)Oil recovery (%) 88 91 92__________________________________________________________________________ *Content of starting olefins having the double bonds at C.sub.2 -C.sub.5 positions in total starting olefins.
EXAMPLE 5
The viscosities of micro-emulsions using C.sub.6 -C.sub.18 IOS-Na used in Example 2 as a surfactant were measured. The micro-emulsions were prepared based on the composition of Sample No. 9, except that cosurfactants were changed and hydroxyethylene cellulose was added in some cases. In all cases, uniform micro-emulsions were formed although the cosurfactants were changed or the thickening agent was added.
The viscosity was measured by using a Brookfield type viscometer at 25.degree. C. The results are shown in Table 5 below.
TABLE 5______________________________________Sample No. 18 19 20 21 22______________________________________Surfactant C.sub.16 -C.sub.18 IOS--NaCosurfactant (%)Amyl alcohol 4.5 3 4.5 4.5 4.5Isopropyl alcohol -- 1.5 -- -- --Hydroxyethyl cellulose -- -- 1000 2000 3000(ppm based on total composition)Viscosity (cp at 25.degree. C.) 28 24 70 89 154______________________________________
REFERENCE EXAMPLE
Micro-emulsions were prepared by using C.sub.14 -C.sub.18 IOS-Na and C.sub.20 -C.sub.24 IOS-Na as a surfactant. The cosurfactants, hydrocarbons, and brine were changed as shown in Table 6. The results are shown in Table 6 below. As is clear from the results shown in Table 6, the micro-emulsions could be formed by using IOS when the compositions were changed.
TABLE 6__________________________________________________________________________Reference Sample No. 1 2 3 4 5 6 7 8__________________________________________________________________________Anionic surfactantC.sub.14 -C.sub.18 ISO--Na 16 -- -- 10.5 -- 10.5 -- --C.sub.20 -C.sub.24 ISO--Na -- 16 10.5 -- 14 -- 10.5 10.5CosurfactantAmyl alcohol 4 4 4.5 -- 6 4.5 4.5 --Isopropyl alcohol -- -- -- 4.5 -- -- -- 4.5HydrocarbonKerosine 16 -- -- 8.5 8 -- -- 25.5Fuel oil -- 16 17 -- -- 17 17 --WaterBrine NaCl 0.5% 64 -- 68 -- -- -- -- 59.5Brine NaCl 2.0% -- -- -- -- -- -- 68 --Brine NaCl 4.0% -- 64 -- 76.5 72 -- -- --Brine NaCl 8.0% -- -- -- -- -- 68 -- --PropertiesVisual appearance o o o o o o o oInterfacial tension (.times. 10.sup.-2 dyne/cm) 0.82 0.09 0.10 0.27 0.95 0.52 0.07 0.07Viscosity (centipoise) 11 21 18 12 42 19 20 19__________________________________________________________________________

Number	Date	Country	Kind
57-10858	Jan 1982	JPX
58-48666	Mar 1983	JPX

Number	Name	Date
3376336	Stein et al.	Apr 1968
3415753	Stein et al.	Dec 1968
3428654	Rubinfeld et al.	Feb 1969
3506070	Jones	Apr 1970
3508611	Davis et al.	Apr 1970
3536136	Jones	Oct 1970
3808156	Gorsich et al.	Apr 1974
3867317	Woo et al.	Feb 1975
3990515	Wilchester et al.	Nov 1976
4064076	Klisch et al.	Dec 1977

Micellar slug for oil recovery

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