CA1246856A - Oil reservoir permeability control using polymeric gels - Google Patents
Oil reservoir permeability control using polymeric gelsInfo
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- CA1246856A CA1246856A CA000508885A CA508885A CA1246856A CA 1246856 A CA1246856 A CA 1246856A CA 000508885 A CA000508885 A CA 000508885A CA 508885 A CA508885 A CA 508885A CA 1246856 A CA1246856 A CA 1246856A
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- 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
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/84—Compositions based on water or polar solvents
- C09K8/86—Compositions based on water or polar solvents containing organic compounds
- C09K8/88—Compositions based on water or polar solvents containing organic compounds macromolecular compounds
- C09K8/90—Compositions based on water or polar solvents containing organic compounds macromolecular compounds of natural origin, e.g. polysaccharides, cellulose
- C09K8/905—Biopolymers
Abstract
OIL RESERVOIR PERMEABILITY CONTROL USING POLYMERIC GELS
ABSTRACT OF THE DISCLOSURE:
The permeability of subterranean oil-bearing formations is selectively reduced by the injection into the formation of the non-xanthan, anionic heteropolysaccharide S-130 produced by fermentation with a microorganism of the Alcaligenes species. The polymer forms shear-thinning, viscous solutions which selectively enter the more highly permeable regions of the formation and form a gel plug in them to reduce their permeability. The polymer forms gels which are stable under a wide range of reservoir conditions including high temperatures.
ABSTRACT OF THE DISCLOSURE:
The permeability of subterranean oil-bearing formations is selectively reduced by the injection into the formation of the non-xanthan, anionic heteropolysaccharide S-130 produced by fermentation with a microorganism of the Alcaligenes species. The polymer forms shear-thinning, viscous solutions which selectively enter the more highly permeable regions of the formation and form a gel plug in them to reduce their permeability. The polymer forms gels which are stable under a wide range of reservoir conditions including high temperatures.
Description
G
OIL RESERV~IR PERMEABILITY CONTROL USING POLYMERIC GELS
This invention relates to polymers which are useful for the control of permeability in subterranean oil-bearing formations and more particularly, to polymers of this ~ind which have improved gel strength, gel consistency and injectivity. The invention also relates to the control of permeability in oil reservoirs using these polymers and to production methods using them.
In the production of oil frGm subterranean oil reservoirs by various flooding techniques, especially waterflooding, it has become a common expedient to add various polymeric thickening agents to the water in order to increase its viscosity to a point where it approaches that of the crude oil which is to be displaced so as to improve the displacement of the oil from the reservoir. The use of polymers for this purpose is often stated to be for mobility control.
Another problem which arises in the various flooding processes is that different strata or zones in the reservoir often possess different permeabilities so that displacing fluids enter the high permeability or "thief" zones in preference to zones of lower permeability where significant quantities of oil may be left unless measures are taken to plug the high permeability zones wholly or partly and so divert the displacing f]uid into the low permeability zones.
Mechanical isolation of the thief zones has been tried but vertical communication among reservoir strata often S~
renders such measures ineffective. Physical plugging of the high permeability ~ones by cements and solid slurries has also been attempted with varying degrees of success, but with this technique the most serious drawback is the possibility of permanently closing still productive horizons.
From these early experiences, the desirability of designing a viscous slug capable of sealing off the most permeable layers so that the floodwater would be diverted to the underswept, tighter regions of the reservoir became evident. This led to the use of oil/water emulsions, gels and polymers for controlling the permeability of the formations in a process frequently referred to as "profile control", a reference to the control of the vertical permeability profile of the reservoir. Profile control agents which have been proposed have included oil/water emulsions, gels, e.g.
lignosulfonate gels and polymers, with polymers being the most extensively applied in recent years.
Among the polymers so far examined for improving waterflood conformance are polyacrylamides, polysaccharides, celluloses, furfural-alcohol and acrylic/epoxy resins, silicates and polyisocyanurates.
A major~part of this work has been conducted with the polyacrylamides. Polyacrylamides have been used both in their normal, non-cross-linked form as well as in the form of cross-linked metal complexes. In either form, the beneficial effects derived from these polyacrylamides seem to dissipate rapidly due to shear degradation during injection and sensitivity to reservoir brines.
Another group of polymeric thickeners which has received considerable attention for use in waterflooding are the polysaccharides, particularly the xanthan ~Z~56 polysaccharides, that is, the polysaccharides produced by the action of bacteria of the genus Xantho onas on carbohydrates. For example, U.S. Patent 3,908,760 describes a polymer waterflooding process in which a gelled, water-soluble Xanthomonas polysaccharide is injected into a stratified reservoir to form a slug, band or front of gel extending vertically across both high permeability and low permeability strata. This patent also suggests the use of complexed polysaccharides to block natural or man-made fractures in formations.
One problem which has continually attended the use of organic polymers as profile control agents is that of stability in the reservoir. This requires not only that the gel formed by the polymer should be stable to the relatively high temperatures which are encountered in some reservoirs-- in itself, a difficult requirement-- but also, that the gel should be stable over as wide a range of pH conditions as possible so that the polymer will have the potential of being used in reservoirs of different kinds, e.g. sandstone, carbonate rock and others. Stability to various oilfield brines is another desirable requirement. Many of the known types of organic gel-forming polymers are unsatisfactory in one respect or another, e.g.
temperature, stability, brine stability, pH range so that there has been a continuing need for new and different polymers for permeability control purposes.
It has now been found that a non-xanthan polysaccharide, the heteropolysaccharide S-130, has properties which make it highly suitable for use in controlling the permeability of subterranean strata.
According to the present invention, there is therefore 5~
provided a method of controlling the permeability of a subterranean, oil-bearing formation which comprises injecting into the formation an aqueous polymeric dispersion or solution of heteropolysaccharide S-130.
Polymer gels are generally used for permeability profile control in oilfield flooding operations for enhanced oil recovery. In flooding operations, a liquid (usually water) is injected into the subterranean, oil-bearing formation through an in~ection well which extends from the surface of the earth down into the formation. A production well also extends into the formation at an offset or horizontal distance from the injection so that J as the flooding liquid is injected into the formation through the injection well, it displaces the oil towards the production well, from which it may be recovered.
Invariably, more than one injection well and more than one production well will be used in order to cover the oilfield adequately and to maximize recovery. Various arrangements of injection and production wells are used to this end, e.g. linear arrangements to form a line drive, five spot, inverted five spot, seven spot, inverted seven spot, all of which are established in conventional practice.
To control the permeability of the subterranean formation, an aqueous solution or dispersion of the polymer is injected into the formation through the injecticn well. The aqueous fluids formed by the polymer are non-Newtonian in behavior and exhibit shear-thinning characteristics. These rheological characteristics of the fluid enable it to pass preferentially into the zones or strata of relatively higher permeability and, having entered them, to form a gel-like plug when the shear conditions prevailing ~2~ 356 during the injection process are removed. Because relatively high shear conditions prevail not only in the injection well as the fluid is being pumped down into the formation but also in the regions of the formation immediately surrounding the injection well, the injected fluid remains in a pumpable, fluid condition in these regions. However, as the injected solution or dispersion of the polymer passes into the regions more distant from the well, the gel sets up in the pores of the formation to reduce its permeability. The initial viscosity of the polymer solution or dispersion prevents it entering the less permeable regions of the formation so that the permeability reduction takes place preferentially in the more highly permeable regions, with the result that after the treatment has been completed, a more uniform permeability is obtained.
The permeability control method using the S-130 polysaccharide as the qel-forming polymer is particularly useful with enhanced recovery processes using a fluid drive such as a waterflood. The permeability control treatment may be carried out periodically, when necessary to achieve the desired permeability profile. The method may also be used to effect control of permeability around a production well for example, by plugging permeable water channels which would otherwise lead to excess water production at the well.
The polymer which is used in the present permeability control process is the non-xanthan heteropolysaccharide S-130. This polysaccharide is produced by the aerobic fermentation of suitable aqueous nutrient media with an organism of the Alcaliqenes species, identified as ATCC 31555 (American Type Culture Collection, Accession No. ATCC 31555, unrestricted permanent deposit made 27 August 1979). The polymer produced by the fermentation of carbohydrate sources of assimilable carbon in the presence of the microorganism is composed principally of carbohydrate, with a small quantity of O-acyl groups. The carbohydrate portion of the polysaccharide contains glucuronic acid and the neutral sugars mannose, glucose and rhamnose in an approximate molar ratio of 1:2:2. The ratio of terminally linked rhamnose to 1,4-linked rhamnose is 1:2, with the glucose being principally 1,3-linked.
Polysaccharide S-130, its characteristic properties, its method of production and the characteristics of the A. s~P. microorganism used in the fermentation are described in greater detail in U.S.
Patent No. 4,342,866. The polysaccharide is available commercially from the Kelco Oil Field Group, division of Merck and Co. Inc., U.S.A.
Polysaccharide S-130 produces high viscosity aqueous solutions which exhibit superior viscosity retention at high temperatures as well as desirable shear-thinning characteristics. Available data indicate that S-130 maintains at least half its room temperature viscosity at a temperature of 300F (about 150C) and that the ~iscosity is stable for relatively long periods at high temperatures. The solutions are highly shear thinning or pseudoplastic; viscosity decreases with increasing shear rate and immediately reverts back to a higher viscosity when shear is reduced. This property enables it to be effectively placed in high permeability portions of subterranean formations so that, when the shear is reduced, a highly viscous gel will be formed to block these regions selectively.
However, the high degree of shear thinning which this polymer exhibits also indicates that in certain s~
instances, care may have to be taken in placing it in the formation. Because solutions of the polymer become almost water-thin at high shear rates, there is a possibility that under these conditions the solution may be capable of entering the less highly permeable regions of the formation where it would plug them when the gel is re-formed. To prevent this from happening, it may be desirable to identify the more highly permeable strata and to inject the polymer solution into these regions alone by the use of suitable packers in the injection well.
The stability of the polymer at relatively high temperatures, particularly above 150 or 165F, is particularly useful in the present invention since it enables the polymer to be used in high temperature reservoirs, e.g. those with temperatures up to 200F
or even higher without the risk of excessive degradation induced by the reservoir temperature. Also, the polymer forms gels which, although stiff enouqh to resist pressure from the flooding liquid, are not so hard as to present the possibility of damage to the reservoir.
S-130 polysaccharide, if available as a dry powder, may be hydrated by being mixed into water with suitable agitation to prevent the formation of lumps.
High shear polymer mixers or eductors or jet hoppers may be used for mixinq. If hydration is delayed, increasing the mixing shear, raising the fluid temperature or both may help overcome delays. If lumps tend to form, an initial slurry of the powder in a non-aqueous solvent such as isopropanol or diesoline may be prepared and the slurry poured into water with agitation, to form a lump-free, viscous solution.
A notable characteristic of S-130 polysaccharide is that it develops a high viscosity in saline waters. The viscosity increase is particularly notable in brines which contain divalent cations such as Ca2 and Mq2+ although high concentrations (more than 10,000 ppm) of the divalent ions should be avoided under highly alkaline conditions (above pH 11) since the polysaccharide may then become unstable. Otherwise, the polymer is stable at temperatures up to 300F (about 150C) between pH 5 and 11. It is unstable above pH
13 and, in addition, if certain cationic surfactants are present, insoluble precipitates may be formed under certain conditions. Simple testing should therefore be carried out to determine whether the polymer will perform satisfactorily under the exact conditions contemplated. The polymer also develops high viscous aqueous solutions in the presence of monovalent cations such as Na+, K+. It may therefore be formulated with many brines and brackish waters including seawater, salines containing, for example, up to 3% KCl, up to 25%
of NaCl or up to 20% CaC12. It may be desirable to prehydrate the polymer in fresh water (distilled water, deionized water or other water essentially free of cations) before mixing with the saline to the desired dilution.
The S-130 polysaccharide may also be cross-linked to form highly viscous solutions by the use of trivalent cations, especially chromium, aluminum and zirconium, although other cations such as iron (III) which are commonly found in oilfield brines will also effect cross-linking. As is the case when highly saline waters containing monovalent and divalent cations are used, it is preferable to prehydrate the polymer using fresh water and then to mix the prehydrated polymer with a solution of the cross-linking cation in order to achieve the desired highly viscous aqueous solution.
35~i Cross-linking may also be effected by the use of organic compounds which contain at least two positively charged nitrogen atoms, for example, the salts of diamines such as ethylene diamine, propylene diamine, butylene diamine or of cyclic diamines such as piperazine.
The polymer is stable over a wide range of pH
values, generally up to pH 13 although, as mentioned above, the presence of certain cations may set a somewhat lower limit on stability. Because of this, the polymer thickened solutions may be used in a wide variety of reservoir formations including, in particular, alkaline formations such as carbonate, where other polymers may have reduced stability. Stability of the gel appears to be favorable at pH values from about 4 to 8, with neutral pH (7.0-7.5) being preferred where acidic cross-linking agents such as Cr (III) are not used. If Cr (III) or other acidic cross-linking agents are used, somewhat lower pH values of 4 to 5 are preferred for maximum gel stability.
The final aqueous solution of the polymer will generally contain from 100 to 10,000 ppmw of the polymer, although normally 1,000 to 5,000 ppmw will normally be used with 1,000-3,000 ppmw being normally preferred for maximum effectiveness. The amount of the solution will normally be from 10 to 100% of the pore volume of the highly permeable regions which are being treated. When a cross-linking agent such as Cr (III) is being used, it will generally be present in an amount of from 0.5 to 10 percent (molar) of the polymer. Thus, if the polymer is present in its normally preferred amount of 1,000-3,000 ppmw, the cross-linking agent will normally be used in an amount of from 5-300 ppmw although normally at least 10 ppmw will be required and B5~;
in most cases at least 25 ppmw will be necessary to ensure a fully developed gel structure. Thus, the content of cross-linking agent will generally be in the range of 25-300 ppmw, referred to fresh water. However, since the polymer is capable of developing highly viscous solutions with saline waters, including those with monovalent cations, divalent cations or both, as mentioned above, it may be possible to use less than these amounts of cross-linking agent if such a saline water is used to formulate the solution.
This invention is illustrated by the following Examples:
Examples 1-24 The anionic polysaccharide biopolymer S-130 in powder form was dispersed at the desired concentration in an oilfield brine by high speed mixing in a blender for about 20 minutes. The composition of the brine is set out in Table 1 below.
Table 1 Brine Composition Cations Anions mg/l mq/I
Sodium60,700 Chlorine119,000 Potassium156 Bicarbonate0 Magnesium1,950 Carbonate 0 Calcium12,100 Sulfate N.D.
Barium 122 Hydroxide 0 Iron 40 Sum75,168 Sum 119,000 Total Dissolved Solids: 194,000 mg/l Specific Gravity at 25C: 1.14739 pH: 4.25 Aliquots (100 ml) of dispersed polymer were further treated with cross-linking agent and NaOH as pH
control agent ~if used) by mixing in a blender cup for about 15 seconds. The mixed samples were immediately placed in closed bottles and placed in an oven at 74C
(165F). The samples were not held under an inert atmosphere but all contained about 400 ppm formaldehyde to prevent microbial degradation.
The cross-linking agents used were Cr (III) as CrC13, piperazine dihydrochloride (PIP-2HCl) and putrescine dihydrochloride (PUT-2HCl; 1,4-butane diamine dihydrochloride), in amounts from 10 to 200 ppm at a polymer concentration of 2,000 ppmw.
The samples were inspected after extended periods of time (1 week and 1 month for Examples 15-24;
OIL RESERV~IR PERMEABILITY CONTROL USING POLYMERIC GELS
This invention relates to polymers which are useful for the control of permeability in subterranean oil-bearing formations and more particularly, to polymers of this ~ind which have improved gel strength, gel consistency and injectivity. The invention also relates to the control of permeability in oil reservoirs using these polymers and to production methods using them.
In the production of oil frGm subterranean oil reservoirs by various flooding techniques, especially waterflooding, it has become a common expedient to add various polymeric thickening agents to the water in order to increase its viscosity to a point where it approaches that of the crude oil which is to be displaced so as to improve the displacement of the oil from the reservoir. The use of polymers for this purpose is often stated to be for mobility control.
Another problem which arises in the various flooding processes is that different strata or zones in the reservoir often possess different permeabilities so that displacing fluids enter the high permeability or "thief" zones in preference to zones of lower permeability where significant quantities of oil may be left unless measures are taken to plug the high permeability zones wholly or partly and so divert the displacing f]uid into the low permeability zones.
Mechanical isolation of the thief zones has been tried but vertical communication among reservoir strata often S~
renders such measures ineffective. Physical plugging of the high permeability ~ones by cements and solid slurries has also been attempted with varying degrees of success, but with this technique the most serious drawback is the possibility of permanently closing still productive horizons.
From these early experiences, the desirability of designing a viscous slug capable of sealing off the most permeable layers so that the floodwater would be diverted to the underswept, tighter regions of the reservoir became evident. This led to the use of oil/water emulsions, gels and polymers for controlling the permeability of the formations in a process frequently referred to as "profile control", a reference to the control of the vertical permeability profile of the reservoir. Profile control agents which have been proposed have included oil/water emulsions, gels, e.g.
lignosulfonate gels and polymers, with polymers being the most extensively applied in recent years.
Among the polymers so far examined for improving waterflood conformance are polyacrylamides, polysaccharides, celluloses, furfural-alcohol and acrylic/epoxy resins, silicates and polyisocyanurates.
A major~part of this work has been conducted with the polyacrylamides. Polyacrylamides have been used both in their normal, non-cross-linked form as well as in the form of cross-linked metal complexes. In either form, the beneficial effects derived from these polyacrylamides seem to dissipate rapidly due to shear degradation during injection and sensitivity to reservoir brines.
Another group of polymeric thickeners which has received considerable attention for use in waterflooding are the polysaccharides, particularly the xanthan ~Z~56 polysaccharides, that is, the polysaccharides produced by the action of bacteria of the genus Xantho onas on carbohydrates. For example, U.S. Patent 3,908,760 describes a polymer waterflooding process in which a gelled, water-soluble Xanthomonas polysaccharide is injected into a stratified reservoir to form a slug, band or front of gel extending vertically across both high permeability and low permeability strata. This patent also suggests the use of complexed polysaccharides to block natural or man-made fractures in formations.
One problem which has continually attended the use of organic polymers as profile control agents is that of stability in the reservoir. This requires not only that the gel formed by the polymer should be stable to the relatively high temperatures which are encountered in some reservoirs-- in itself, a difficult requirement-- but also, that the gel should be stable over as wide a range of pH conditions as possible so that the polymer will have the potential of being used in reservoirs of different kinds, e.g. sandstone, carbonate rock and others. Stability to various oilfield brines is another desirable requirement. Many of the known types of organic gel-forming polymers are unsatisfactory in one respect or another, e.g.
temperature, stability, brine stability, pH range so that there has been a continuing need for new and different polymers for permeability control purposes.
It has now been found that a non-xanthan polysaccharide, the heteropolysaccharide S-130, has properties which make it highly suitable for use in controlling the permeability of subterranean strata.
According to the present invention, there is therefore 5~
provided a method of controlling the permeability of a subterranean, oil-bearing formation which comprises injecting into the formation an aqueous polymeric dispersion or solution of heteropolysaccharide S-130.
Polymer gels are generally used for permeability profile control in oilfield flooding operations for enhanced oil recovery. In flooding operations, a liquid (usually water) is injected into the subterranean, oil-bearing formation through an in~ection well which extends from the surface of the earth down into the formation. A production well also extends into the formation at an offset or horizontal distance from the injection so that J as the flooding liquid is injected into the formation through the injection well, it displaces the oil towards the production well, from which it may be recovered.
Invariably, more than one injection well and more than one production well will be used in order to cover the oilfield adequately and to maximize recovery. Various arrangements of injection and production wells are used to this end, e.g. linear arrangements to form a line drive, five spot, inverted five spot, seven spot, inverted seven spot, all of which are established in conventional practice.
To control the permeability of the subterranean formation, an aqueous solution or dispersion of the polymer is injected into the formation through the injecticn well. The aqueous fluids formed by the polymer are non-Newtonian in behavior and exhibit shear-thinning characteristics. These rheological characteristics of the fluid enable it to pass preferentially into the zones or strata of relatively higher permeability and, having entered them, to form a gel-like plug when the shear conditions prevailing ~2~ 356 during the injection process are removed. Because relatively high shear conditions prevail not only in the injection well as the fluid is being pumped down into the formation but also in the regions of the formation immediately surrounding the injection well, the injected fluid remains in a pumpable, fluid condition in these regions. However, as the injected solution or dispersion of the polymer passes into the regions more distant from the well, the gel sets up in the pores of the formation to reduce its permeability. The initial viscosity of the polymer solution or dispersion prevents it entering the less permeable regions of the formation so that the permeability reduction takes place preferentially in the more highly permeable regions, with the result that after the treatment has been completed, a more uniform permeability is obtained.
The permeability control method using the S-130 polysaccharide as the qel-forming polymer is particularly useful with enhanced recovery processes using a fluid drive such as a waterflood. The permeability control treatment may be carried out periodically, when necessary to achieve the desired permeability profile. The method may also be used to effect control of permeability around a production well for example, by plugging permeable water channels which would otherwise lead to excess water production at the well.
The polymer which is used in the present permeability control process is the non-xanthan heteropolysaccharide S-130. This polysaccharide is produced by the aerobic fermentation of suitable aqueous nutrient media with an organism of the Alcaliqenes species, identified as ATCC 31555 (American Type Culture Collection, Accession No. ATCC 31555, unrestricted permanent deposit made 27 August 1979). The polymer produced by the fermentation of carbohydrate sources of assimilable carbon in the presence of the microorganism is composed principally of carbohydrate, with a small quantity of O-acyl groups. The carbohydrate portion of the polysaccharide contains glucuronic acid and the neutral sugars mannose, glucose and rhamnose in an approximate molar ratio of 1:2:2. The ratio of terminally linked rhamnose to 1,4-linked rhamnose is 1:2, with the glucose being principally 1,3-linked.
Polysaccharide S-130, its characteristic properties, its method of production and the characteristics of the A. s~P. microorganism used in the fermentation are described in greater detail in U.S.
Patent No. 4,342,866. The polysaccharide is available commercially from the Kelco Oil Field Group, division of Merck and Co. Inc., U.S.A.
Polysaccharide S-130 produces high viscosity aqueous solutions which exhibit superior viscosity retention at high temperatures as well as desirable shear-thinning characteristics. Available data indicate that S-130 maintains at least half its room temperature viscosity at a temperature of 300F (about 150C) and that the ~iscosity is stable for relatively long periods at high temperatures. The solutions are highly shear thinning or pseudoplastic; viscosity decreases with increasing shear rate and immediately reverts back to a higher viscosity when shear is reduced. This property enables it to be effectively placed in high permeability portions of subterranean formations so that, when the shear is reduced, a highly viscous gel will be formed to block these regions selectively.
However, the high degree of shear thinning which this polymer exhibits also indicates that in certain s~
instances, care may have to be taken in placing it in the formation. Because solutions of the polymer become almost water-thin at high shear rates, there is a possibility that under these conditions the solution may be capable of entering the less highly permeable regions of the formation where it would plug them when the gel is re-formed. To prevent this from happening, it may be desirable to identify the more highly permeable strata and to inject the polymer solution into these regions alone by the use of suitable packers in the injection well.
The stability of the polymer at relatively high temperatures, particularly above 150 or 165F, is particularly useful in the present invention since it enables the polymer to be used in high temperature reservoirs, e.g. those with temperatures up to 200F
or even higher without the risk of excessive degradation induced by the reservoir temperature. Also, the polymer forms gels which, although stiff enouqh to resist pressure from the flooding liquid, are not so hard as to present the possibility of damage to the reservoir.
S-130 polysaccharide, if available as a dry powder, may be hydrated by being mixed into water with suitable agitation to prevent the formation of lumps.
High shear polymer mixers or eductors or jet hoppers may be used for mixinq. If hydration is delayed, increasing the mixing shear, raising the fluid temperature or both may help overcome delays. If lumps tend to form, an initial slurry of the powder in a non-aqueous solvent such as isopropanol or diesoline may be prepared and the slurry poured into water with agitation, to form a lump-free, viscous solution.
A notable characteristic of S-130 polysaccharide is that it develops a high viscosity in saline waters. The viscosity increase is particularly notable in brines which contain divalent cations such as Ca2 and Mq2+ although high concentrations (more than 10,000 ppm) of the divalent ions should be avoided under highly alkaline conditions (above pH 11) since the polysaccharide may then become unstable. Otherwise, the polymer is stable at temperatures up to 300F (about 150C) between pH 5 and 11. It is unstable above pH
13 and, in addition, if certain cationic surfactants are present, insoluble precipitates may be formed under certain conditions. Simple testing should therefore be carried out to determine whether the polymer will perform satisfactorily under the exact conditions contemplated. The polymer also develops high viscous aqueous solutions in the presence of monovalent cations such as Na+, K+. It may therefore be formulated with many brines and brackish waters including seawater, salines containing, for example, up to 3% KCl, up to 25%
of NaCl or up to 20% CaC12. It may be desirable to prehydrate the polymer in fresh water (distilled water, deionized water or other water essentially free of cations) before mixing with the saline to the desired dilution.
The S-130 polysaccharide may also be cross-linked to form highly viscous solutions by the use of trivalent cations, especially chromium, aluminum and zirconium, although other cations such as iron (III) which are commonly found in oilfield brines will also effect cross-linking. As is the case when highly saline waters containing monovalent and divalent cations are used, it is preferable to prehydrate the polymer using fresh water and then to mix the prehydrated polymer with a solution of the cross-linking cation in order to achieve the desired highly viscous aqueous solution.
35~i Cross-linking may also be effected by the use of organic compounds which contain at least two positively charged nitrogen atoms, for example, the salts of diamines such as ethylene diamine, propylene diamine, butylene diamine or of cyclic diamines such as piperazine.
The polymer is stable over a wide range of pH
values, generally up to pH 13 although, as mentioned above, the presence of certain cations may set a somewhat lower limit on stability. Because of this, the polymer thickened solutions may be used in a wide variety of reservoir formations including, in particular, alkaline formations such as carbonate, where other polymers may have reduced stability. Stability of the gel appears to be favorable at pH values from about 4 to 8, with neutral pH (7.0-7.5) being preferred where acidic cross-linking agents such as Cr (III) are not used. If Cr (III) or other acidic cross-linking agents are used, somewhat lower pH values of 4 to 5 are preferred for maximum gel stability.
The final aqueous solution of the polymer will generally contain from 100 to 10,000 ppmw of the polymer, although normally 1,000 to 5,000 ppmw will normally be used with 1,000-3,000 ppmw being normally preferred for maximum effectiveness. The amount of the solution will normally be from 10 to 100% of the pore volume of the highly permeable regions which are being treated. When a cross-linking agent such as Cr (III) is being used, it will generally be present in an amount of from 0.5 to 10 percent (molar) of the polymer. Thus, if the polymer is present in its normally preferred amount of 1,000-3,000 ppmw, the cross-linking agent will normally be used in an amount of from 5-300 ppmw although normally at least 10 ppmw will be required and B5~;
in most cases at least 25 ppmw will be necessary to ensure a fully developed gel structure. Thus, the content of cross-linking agent will generally be in the range of 25-300 ppmw, referred to fresh water. However, since the polymer is capable of developing highly viscous solutions with saline waters, including those with monovalent cations, divalent cations or both, as mentioned above, it may be possible to use less than these amounts of cross-linking agent if such a saline water is used to formulate the solution.
This invention is illustrated by the following Examples:
Examples 1-24 The anionic polysaccharide biopolymer S-130 in powder form was dispersed at the desired concentration in an oilfield brine by high speed mixing in a blender for about 20 minutes. The composition of the brine is set out in Table 1 below.
Table 1 Brine Composition Cations Anions mg/l mq/I
Sodium60,700 Chlorine119,000 Potassium156 Bicarbonate0 Magnesium1,950 Carbonate 0 Calcium12,100 Sulfate N.D.
Barium 122 Hydroxide 0 Iron 40 Sum75,168 Sum 119,000 Total Dissolved Solids: 194,000 mg/l Specific Gravity at 25C: 1.14739 pH: 4.25 Aliquots (100 ml) of dispersed polymer were further treated with cross-linking agent and NaOH as pH
control agent ~if used) by mixing in a blender cup for about 15 seconds. The mixed samples were immediately placed in closed bottles and placed in an oven at 74C
(165F). The samples were not held under an inert atmosphere but all contained about 400 ppm formaldehyde to prevent microbial degradation.
The cross-linking agents used were Cr (III) as CrC13, piperazine dihydrochloride (PIP-2HCl) and putrescine dihydrochloride (PUT-2HCl; 1,4-butane diamine dihydrochloride), in amounts from 10 to 200 ppm at a polymer concentration of 2,000 ppmw.
The samples were inspected after extended periods of time (1 week and 1 month for Examples 15-24;
2 wee~s and 5 weeks for Examples 1-14) for syneresis, i.e. gel separation. The degree of syneresis was estimated visually as the proportion by volume of separated water; the nature of the gel was also evaluated and noted.
1;~4~85G
The results are shown in Table 2 below.
Table 2 Biopolymer St,ability at 74C
l-week Cross- Crosslinker Syneresis, Syneresis, Ex. linker conc., ppm PH % , _ % Comments 1 None 0 5.65 (1~10 (2) Good gel 2 None 0 7.11 (1) 1 (2) Rigid gel
1;~4~85G
The results are shown in Table 2 below.
Table 2 Biopolymer St,ability at 74C
l-week Cross- Crosslinker Syneresis, Syneresis, Ex. linker conc., ppm PH % , _ % Comments 1 None 0 5.65 (1~10 (2) Good gel 2 None 0 7.11 (1) 1 (2) Rigid gel
3 None 7-51 (1) 1 (2) Rigid gel
4 None 0 8.01 (1~ 2 (2) Rigid gel . None 0 9.015 (1~15 (2) Stiff gel 6 Cr(III)25 4.32 (1~ 2 (2) Good gel 7 Cr(III)25 7.110 (1)10 (2) Stiff gel 8 Cr(III)25 8.010 (1~10 (2) Stiff gel 9 Cr(III)25 8.615 (1~15 (2) Stiff gel Cr(III)25 9.020 (1)20 (2) Stiff gel 11 Cr(III)50 4.02 (1) 2 (2) Good gel 12 Cr(III)50 7.05 (1) 8 (2) Stiff gel 13 Cr(III)50 8.110 (1)10 (2~ Stiff gel 14 Cr(III)50 9.010 (1)10 (2) Stiff gel PIP-2HC110 8.0 5 10 Stiff gel 16 PIP-2HC125 8.0 2 2 Stiff gel 17 PIP-2HC150 8.0 2 2 Stiff gel 18 PIP-2~C1100 8.0 2 2 Stiff gel 19 PIP-2HC1200 8.0 1 1 Stiff gel PUT-2HC110 8.0 2 10 Stiff gel 21 PUT-2HC125 8.0 5 10 Rigid gel 22 PUT-2HC150 8.0 5 10 Rigid gel 23 PUT-2HC1100 8.0 5 10 Rigid gel 24 PUT-2HC1200 8.0 5 10 Rigid gel Notes (1) 2 week syneresis period (2) 5 week syneresis period Examples 25-37 The procedure of Examples 1-24 was used but with a polymer concentration of 3,000 ppmw and with varying pH values and cross-linking agents as noted with s~
the results in Table 3 below. Samples were again held at 74C for periods of 2 and 5 weeks.
Table 3 Biopolymer Stability at 74C
l-week Cross- Crosslinker Syneresis, SynerPsis, Ex. linker conc., ppm ~ %. 2 Weeks %, 5 Weeks Comments None 0 5.115 30 Good gel 26 None 0 7.025 25 Stiff gel 27 None 0 8.015 20 Stiff gel 28 None 0 9.025 25 Stiff gel 29 Cr(III)25 4~810 30 Good gel Cr(III~25 6.110 10 Stiff gel 31 Cr(III)25 7.115 20 Stiff gel 32 Cr(III)25 8.120 20 Stiff gel 33 Cr(III)25 9.020 25 Stiff gel 34 Cr(III~50 4.320 60 Good gel Cr(III)50 6.120 30 Stiff gel 36 Cr(III)50 7.115 15 Stiff gel 37 Cr(III)50 8.020 20 Stiff gel Examples 38-42 The procedure of Examples 1-24 was again followed but a holding temperature of 93C (200F) was used with a polymer concentration of 2,000 ppmw.
The results are shown in Table 4 below, for syneresis periods of 2 and 5 weeks.
Table 4 BiopolYmer Stability at 93QC
~ l-week Cross- Crosslinker Syneresis, Syneresis, Ex. linker conc., ppm PH %, 2 Weeks %. 5 Weeks Comments 38 None 0 4.81 1 Good gel 39 None 0 7.21 2 Good gel None 0 8.02 2 P~igid gel 41 Cr(III)25 7.05 5 Stiff gel 42 Cr(III)25 8.05 5 Stiff gel ~s~s6 _amples 43-46 The procedure of Examples 1-24 was used again but with a polymer concentration of 4,000 ppmw. The results are shown in Table 5 below, for syneresis periods of 1 month, 2 months and 2 1/2 months.
Table 5 Biopolymer Stability at 74C
Cross-Cross- linker Syn. %, Syn. %, Syn. %, Ex. linker Conc ppm pH 1 mo. 2 mos. 2 1~/2 mos. Comments 43 None 0 - - 2 5 Very stiff 44 None 0 7.1 1010 15 Stiff gel 45 Cr(III) 50 8.5 3030 30 Rigid gel 46 Cr(III3 50 4.5 20 20 25 Very stiff
the results in Table 3 below. Samples were again held at 74C for periods of 2 and 5 weeks.
Table 3 Biopolymer Stability at 74C
l-week Cross- Crosslinker Syneresis, SynerPsis, Ex. linker conc., ppm ~ %. 2 Weeks %, 5 Weeks Comments None 0 5.115 30 Good gel 26 None 0 7.025 25 Stiff gel 27 None 0 8.015 20 Stiff gel 28 None 0 9.025 25 Stiff gel 29 Cr(III)25 4~810 30 Good gel Cr(III~25 6.110 10 Stiff gel 31 Cr(III)25 7.115 20 Stiff gel 32 Cr(III)25 8.120 20 Stiff gel 33 Cr(III)25 9.020 25 Stiff gel 34 Cr(III~50 4.320 60 Good gel Cr(III)50 6.120 30 Stiff gel 36 Cr(III)50 7.115 15 Stiff gel 37 Cr(III)50 8.020 20 Stiff gel Examples 38-42 The procedure of Examples 1-24 was again followed but a holding temperature of 93C (200F) was used with a polymer concentration of 2,000 ppmw.
The results are shown in Table 4 below, for syneresis periods of 2 and 5 weeks.
Table 4 BiopolYmer Stability at 93QC
~ l-week Cross- Crosslinker Syneresis, Syneresis, Ex. linker conc., ppm PH %, 2 Weeks %. 5 Weeks Comments 38 None 0 4.81 1 Good gel 39 None 0 7.21 2 Good gel None 0 8.02 2 P~igid gel 41 Cr(III)25 7.05 5 Stiff gel 42 Cr(III)25 8.05 5 Stiff gel ~s~s6 _amples 43-46 The procedure of Examples 1-24 was used again but with a polymer concentration of 4,000 ppmw. The results are shown in Table 5 below, for syneresis periods of 1 month, 2 months and 2 1/2 months.
Table 5 Biopolymer Stability at 74C
Cross-Cross- linker Syn. %, Syn. %, Syn. %, Ex. linker Conc ppm pH 1 mo. 2 mos. 2 1~/2 mos. Comments 43 None 0 - - 2 5 Very stiff 44 None 0 7.1 1010 15 Stiff gel 45 Cr(III) 50 8.5 3030 30 Rigid gel 46 Cr(III3 50 4.5 20 20 25 Very stiff
Claims (27)
1. A method for the selective control of permeability in a subterranean oil-bearing formation which comprises injecting into the formation a viscous solution of the non-xanthan, anionic heteropolysaccharide S-130.
2. A method according to claim 1 in which the solution comprises an aqueous solution.
3. A method according to claim 2 in which the solution contains from 1,000 to 5,000 ppmw of the heteropolysaccharide.
4. A method according to claim 3 in which the solution contains from 1,000 to 3,000 ppmw of the heteropolysaccharide.
5. A method according to claim 2 in which the solution contains monovalent cations.
6. A method according to claim 2 in which the solution contains divalent cations.
7. A method according to claim 2 in which the solution contains trivalent cations.
8. A method according to claim 7 in which the cations are cations of chromium (III).
9. A method according to claim 2 in which the solution contains cations of basic organic compounds, the cations containing at least two positively charged centers.
10. A method according to claim 8 in which the cations are cations of an organic diamine.
11. A method according to claim 1 in which the heteropolysaccharide S-130 is produced by fermentation of a microorganism of the Alcaligenes species in an aqueous nutrient medium.
12. In a method for the enhanced recovery of oil by the injection of a flooding fluid into a subterranean oil-bearing formation through an injection well extending from the surface of the earth into the formation, to displace oil from the formation towards a production well at a distance from the injection well, the improvement which is characterized in selectively controlling the permeability of the formation by injecting into the formation through the injection well a solution of the non-xanthan, anionic heteropolysaccharide S-130 to selectively reduce the permeability of the more highly permeable regions of the formation.
13. A method according to claim 12 in which the solution comprises an aqueous solution.
14. A method according to claim 13 in which the solution contains from 1,000 to 5,000 ppmw of the heteropolysaccharide.
15. A method according to claim 14 in which the solution contains from 1,000 to 3,000 ppmw of the heteropolysaccharide.
16. A method according to claim 13 in which the solution contains monovalent cations.
17. A method according to claim 13 in which the solution contains divalent cations.
18. A method according to claim 13 in which the solution contains trivalent cations.
19. A method according to claim 18 in which the cations are cations of chromium (III).
20. A method according to claim 13 in which the solution contains cations of basic organic compounds, the cations containing at least two positively charged centers.
21. A method according to claim 19 in which the cations are cations of an organic diamine.
22. A method according to claim 13 in which the solution of the heteropolysaccharide is prepared by hydrating the heteropolysaccharide in fresh water and adding to the hydrated heteropolysaccharide a cross-linking agent for the heteropolysaccharide.
23. A method according to claim 22 in which the cross-linking agent comprises a salt of a trivalent metal.
24. A method according to claim 23 in which the trivalent metal is chromium (III).
25. A method according to claim 24 in which the concentration of the heteropolysaccharide in the final solution is from 1,000 to 3,000 ppmw and the concentration of chromium (III) is from 25 to 100 ppmw as Cr.
26. A method according to claim 12 in which the amount of the solution is from 10 to 100% of the pore volume of the more highly permeable regions of the formation which are to be treated.
27. A method according to claim 12 in which the heteropolysaccharide S-130 is produced by fermentation of a microorganism of the Alcaligenes species in an aqueous nutrient medium.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US737,617 | 1985-05-24 | ||
| US06/737,617 US4658898A (en) | 1985-05-24 | 1985-05-24 | Oil reservoir permeability control using polymeric gels |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1246856A true CA1246856A (en) | 1988-12-20 |
Family
ID=24964595
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000508885A Expired CA1246856A (en) | 1985-05-24 | 1986-05-12 | Oil reservoir permeability control using polymeric gels |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US4658898A (en) |
| EP (1) | EP0202935B1 (en) |
| CA (1) | CA1246856A (en) |
| DE (1) | DE3677411D1 (en) |
| NO (1) | NO173346C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7677313B2 (en) | 2004-09-15 | 2010-03-16 | Alberta Science And Research Authority | Method for controlling water influx into wellbores by blocking high-permeability channels |
Families Citing this family (32)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2586750B1 (en) * | 1985-08-29 | 1988-05-20 | Inst Francais Du Petrole | PROCESS FOR PREVENTING THE COMING OF WATER IN AN OIL AND / OR GAS PRODUCING WELL |
| US4809782A (en) * | 1985-09-25 | 1989-03-07 | Mobil Oil Corporation | Block copolymers useful for enhanced oil recovery processes |
| US4834180A (en) * | 1986-10-09 | 1989-05-30 | Mobil Oil Corporation | Amino resins crosslinked polymer gels for permeability profile control |
| US4787451A (en) * | 1986-12-11 | 1988-11-29 | Mobil Oil Corporation | Melamine/formaldehyde cross-linking of polymers for profile control |
| US4906575A (en) * | 1987-03-06 | 1990-03-06 | Chevron Research Company | Phosphate compound that is used in a microbial profile modification process |
| US4799545A (en) * | 1987-03-06 | 1989-01-24 | Chevron Research Company | Bacteria and its use in a microbial profile modification process |
| US4947932A (en) * | 1987-03-06 | 1990-08-14 | Chevron Research Company | Phosphate compound that is used in a microbial profile modification process |
| US4793416A (en) * | 1987-06-30 | 1988-12-27 | Mobile Oil Corporation | Organic crosslinking of polymers for CO2 flooding profile control |
| WO1989008768A1 (en) * | 1988-03-10 | 1989-09-21 | Institutt For Kontinentalsokkelundersøkelser Og Pe | Method for enhanced recovery of hydrocarbone |
| US4809781A (en) * | 1988-03-21 | 1989-03-07 | Mobil Oil Corporation | Method for selectively plugging highly permeable zones in a subterranean formation |
| US4991652A (en) * | 1988-12-12 | 1991-02-12 | Mobil Oil Corporation | Oil reservoir permeability profile control with crosslinked welan gum biopolymers |
| US4981520A (en) * | 1988-12-12 | 1991-01-01 | Mobil Oil Corporation | Oil reservoir permeability profile control with crosslinked welan gum biopolymers |
| US4907656A (en) * | 1988-12-30 | 1990-03-13 | Mobil Oil Corporation | Method for preventing steam channelling into a non-aquifer bottom water zone |
| US5071890A (en) * | 1989-01-03 | 1991-12-10 | Mobil Oil Corp. | Composition for selective placement of polymer gels for profile control in thermal oil recovery |
| US4940091A (en) * | 1989-01-03 | 1990-07-10 | Mobil Oil Corporation | Method for selectively plugging a zone having varying permeabilities with a temperature activated gel |
| US4903768A (en) * | 1989-01-03 | 1990-02-27 | Mobil Oil Corporation | Method for profile control of enhanced oil recovery |
| US4950698A (en) * | 1989-01-03 | 1990-08-21 | Mobil Oil Corporation | Composition for selective placement of polymer gels for profile control in thermal oil recovery |
| US4928766A (en) * | 1989-02-16 | 1990-05-29 | Mobil Oil Corporation | Stabilizing agent for profile control gels and polymeric gels of improved stability |
| US5028344A (en) * | 1989-02-16 | 1991-07-02 | Mobil Oil Corporation | Stabilizing agent for profile control gels and polymeric gels of improved stability |
| IT1229226B (en) * | 1989-03-31 | 1991-07-26 | Eniricerche S P A Agip S P A | PROCEDURE AND COMPOSITION TO REDUCE THE PERMEABILITY OF A HIGH PERMEABILITY AREA IN A PETROLEUM FIELD. |
| US4941533A (en) * | 1989-05-16 | 1990-07-17 | The University Of Kansas | Subterranean permeability modification by using microbial polysaccharide polymers |
| US4962814A (en) * | 1989-09-28 | 1990-10-16 | Mobil Oil Corporation | Optimization of cyclic steam in a reservoir with inactive bottom water |
| US5086089A (en) * | 1989-11-03 | 1992-02-04 | Mobil Oil Corporation | Programmed gelation of polymers using melamine resins |
| US4964461A (en) * | 1989-11-03 | 1990-10-23 | Mobil Oil Corporation | Programmed gelation of polymers using melamine resins |
| US5016713A (en) * | 1990-03-14 | 1991-05-21 | Mobil Oil Corporation | Method of preheating a heavy oil zone through existing bottom water and then diverting steam into the oil zone |
| GB9015913D0 (en) * | 1990-07-19 | 1990-09-05 | Land & Marine Eng Ltd | Thermally insulating compositions and a method of insulating pipeline bundles and pipeline riser caissons |
| US5277830A (en) * | 1990-12-17 | 1994-01-11 | Mobil Oil Corporation | pH tolerant heteropolysaccharide gels for use in profile control |
| US5156214A (en) * | 1990-12-17 | 1992-10-20 | Mobil Oil Corporation | Method for imparting selectivity to polymeric gel systems |
| US5290768A (en) * | 1991-01-18 | 1994-03-01 | Merck & Co., Inc. | Welan gum-ethylene glycol insulating compositions |
| CA2071711A1 (en) * | 1991-06-28 | 1992-12-29 | Todd Talashek | Enhanced solubility of welan gum in ethylene glycol |
| BRPI1011996A2 (en) * | 2009-06-04 | 2016-05-10 | Rhodia Operations | methods and compositions for viscosifying heavy aqueous brine |
| WO2014130250A2 (en) | 2013-02-22 | 2014-08-28 | Conocophillips Company | Low ph crossslinking of polymers |
Family Cites Families (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2390770A (en) * | 1942-10-10 | 1945-12-11 | Sun Oil Co | Method of producing petroleum |
| US3208524A (en) * | 1960-09-26 | 1965-09-28 | Exxon Production Research Co | Process for controlling lost circulation |
| US3779315A (en) * | 1972-08-29 | 1973-12-18 | Phillips Petroleum Co | Production method |
| US3908760A (en) * | 1973-10-09 | 1975-09-30 | Phillips Petroleum Co | Method of treating subterranean formations with aqueous gels |
| US4009755A (en) * | 1976-03-17 | 1977-03-01 | Union Oil Company Of California | Selectively controlling the flow of fluids through subterranean formations |
| US4078607A (en) * | 1976-09-13 | 1978-03-14 | Texaco Inc. | Oil recovery process using improved thickened aqueous flooding liquids |
| US4342866A (en) * | 1979-09-07 | 1982-08-03 | Merck & Co., Inc. | Heteropolysaccharide S-130 |
| CA1173771A (en) * | 1980-05-21 | 1984-09-04 | Roger E. Cripps | Fluid displacement with heteropolysaccharide solutions, and the microbial production of heteropolysaccharides |
| FR2488909A1 (en) * | 1980-08-19 | 1982-02-26 | Shell Int Research | PRODUCTION OF MICROBIAL POLYSACCHARIDES |
| US4458753A (en) * | 1982-10-15 | 1984-07-10 | Pfizer Inc. | Stabilizing polysaccharide solutions for tertiary oil recovery at elevated temperature with borohydride |
| US4552217A (en) * | 1984-07-09 | 1985-11-12 | Phillips Petroleum Company | Microbiocidal anionic sequesterants with polyvalent metal cations for permeability correction process |
| US4613631A (en) * | 1985-05-24 | 1986-09-23 | Mobil Oil Corporation | Crosslinked polymers for enhanced oil recovery |
-
1985
- 1985-05-24 US US06/737,617 patent/US4658898A/en not_active Expired - Fee Related
-
1986
- 1986-05-12 CA CA000508885A patent/CA1246856A/en not_active Expired
- 1986-05-22 EP EP86303878A patent/EP0202935B1/en not_active Expired
- 1986-05-22 DE DE8686303878T patent/DE3677411D1/en not_active Expired - Fee Related
- 1986-05-22 NO NO862049A patent/NO173346C/en unknown
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7677313B2 (en) | 2004-09-15 | 2010-03-16 | Alberta Science And Research Authority | Method for controlling water influx into wellbores by blocking high-permeability channels |
Also Published As
| Publication number | Publication date |
|---|---|
| EP0202935A2 (en) | 1986-11-26 |
| US4658898A (en) | 1987-04-21 |
| DE3677411D1 (en) | 1991-03-14 |
| EP0202935B1 (en) | 1991-02-06 |
| NO173346B (en) | 1993-08-23 |
| NO862049L (en) | 1986-11-25 |
| NO173346C (en) | 1993-12-01 |
| EP0202935A3 (en) | 1988-08-31 |
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