Foamlike Dispersions for Mobility Control in CO2 Floods

1985 ◽  
Vol 25 (04) ◽  
pp. 603-613 ◽  
Author(s):  
John P. Heller ◽  
Cheng Li Lien ◽  
Murty S. Kuntamukkula

Heller, John P., SPE, New Mexico Petroleum Recovery Research Center Petroleum Recovery Research Center Lien, Cheng Li, SPE, New Mexico Petroleum Recovery Research Center, Kuntamukkula, Murty S., SPE, New Mexico Petroleum Recovery Research Center Petroleum Recovery Research Center AUGUST 1985 Abstract At the reservoir temperature and pressure at which CO2 can displace a crude oil with high microscopic-displacement efficiency, its density and compressibility are close to those of the crude oil-and not greatly different from those of water itself. Because of this, the mechanical and chemical characteristics of a high-pressure, CO2-in-water "foam" cannot be assumed to be the same as those of an air/water foam at near-atmospheric pressure. pressure. This paper reports information on the mobility of foamlike dispersions in reservoir rock. The data come both from the recalculation of selected experimental work reported in the literature and from new experiments. An important criterion for these experiments is to eliminate or greatly reduce the influence of fluid compressibility, so as to approximate field conditions in CO2 floods more closely. The core flow experiments performed for this work meet this condition by use of the nonaqueous phase of either liquid CO2 at high pressure, or a light hydrocarbon to simulate dense CO2 in experiments performed at low pressure. We postulate that to be effective in retarding the growth of fingers or other instability patterns in CO2 floods while maintaining a high microscopic displacement efficiency, a foamlike dispersion of dense CO2 in surfactant/water should have the following characteristics. 1. Its aqueous-phase content should be as low as possible, to minimize oil trapping and to permit maximum possible, to minimize oil trapping and to permit maximum contact between CO2 and the crude oil. 2. Its effective mobility in the reservoir rock should be adjustable, by some parameters accessible during its generation, to about that of the oil bank it is expected to form and to displace. Introduction Since the classical flow and model experiments, and calculations of the 1950's and 1960's, it has been well known that adverse mobility ratio prevents the attainment of high areal sweep efficiencies in both miscible and immiscible displacements. The mechanism responsible for this is the formation of "fingers" of an unstable displacement front, which leads to early breakthrough and lowered oil production rates. The only apparent remedy is to thicken or to decrease the mobility of the injected fluids. An early suggestion along this line was to use foams to displace the oil. Several dozen papers over the intervening years have studied this idea further in both laboratory and field, and there is general agreement that the method holds great promise for selected plugging or diversion of flow from high-permeability streaks. Although the literature points out that large pressure drops ate required to move foam through porous media, and although this is very promising for mobility control, serious questions remain unresolved for that application. One such problem is that in most of the reported experiments, considerable expansion in volume occurred over the length of the flow system. Thus, it is difficult to separate the effects of the foam's compressibility from its inherent flow-resisting properties. An even more fundamental question concerns the mechanism of foam flow itself and the task of describing it quantitatively. We reject the idea that a useful description can be given in terms of a "foam viscosity" as measured in any standard viscometer. To explain this view, and to justify a more modest description in terms only of measurable quantities, we present a section on the rheological background of the problem. problem. This work is directed specifically toward the development of foamlike dispersions of dense CO2 in aqueous surfactant solutions for use in the control of mobility ratio in CO2 floods. We have searched the literature for applicable information, and have re-examined several studies of foam flow in porous media. In most cases the given results have been recalculated to cast them all into a common form that, it is hoped, offers a basis for calculation of the pressure gradients associated with foam flow in a reservoir. This paper also contains the results of original, steady-state experiments, performed under approximate field conditions and designed to permit the calculation of the mobility of foam-like dispersions of CO2 in reservoir rock. Finally, some general conclusions are drawn concerning the use of such foams for mobility control. Rheological Background The concept of "viscosity" to represent the resistance offered by a fluid to continuous deformation under the influence of shearing force has been a cornerstone of classical fluid mechanics and is of paramount importance in engineering practice involving fluid flow. The viscosity of a fluid is given by the ratio of shear stress to the rate of shear and is generally a strong function of temperature and weakly dependent on pressure. SPEJ p. 603

1985 ◽  
Vol 25 (05) ◽  
pp. 679-686 ◽  
Author(s):  
J.P. Heller ◽  
D.K. Dandge ◽  
R.J. Card ◽  
L.G. Donaruma

Heller, J.P.; SPE, New Mexico Petroleum Recovery Research Center Dandge, D.K.; New Mexico Petroleum Recovery Research Center Card, R.J.; American Cyanamid Corp. Donaruma, L.G.; Polytechnical Inst. of New York Polytechnical Inst. of New York October 1985 Abstract This paper describes efforts in an experimental search for polymers that are sufficiently soluble in dense CO2 that polymers that are sufficiently soluble in dense CO2 that they could serve as mobility control agents. The operation of the apparatus designed and built for the measurement of solubility in condensed gases is described. A modified version of this apparatus has been used to measure viscosity by timing the fall of a cylinder in a tube. More than a dozen polymers have been found that are soluble at least in the parts-per-thousand (ppt) range in liquid and in dense supercritical CO2. As pressures and temperatures are varied. the solubilities of these polymers generally are found to increase with increasing CO2 density. Certain generalizations have been made concerning the influence of various polymer properties on their solubility in dense CO2. These properties include structure, stereochemistry, and molecular weight. Although the viscosity enhancements of the solutions measured thus far are insufficient for purposes of mobility control, they provide clues that point toward those features of polymer provide clues that point toward those features of polymer molecules that yield greater thickening properties. Also discussed are considerations involved in the application of direct thickeners in the mobility control of CO2 floods and the advantages in the use of such CO2-soluble polymers in place of methods that involve the injection of water. Introduction There is a considerable degree of optimism about the usefulness of CO2 as a displacing agent in EOR operations. At the moderately high pressures and reasonable temperatures common in many oil reservoirs, CO2 is capable of extracting enough of the light ends, in the region of its contact with the crude oil. that a highly efficient displacement in porous media is possible in the laboratory, especially in thin-tube tests. This multiple-contact miscibility, which has been observed in many laboratories, occurs above a threshold minimal miscibility pressure. The higher density attained by CO2 in this pressure. The higher density attained by CO2 in this range has been specifically referred to by Holm and Josendal and by Orr et al. The effectiveness of CO2 in displacing oil from reservoirs is marred, however, by its extremely low viscosity. The viscosity of dense CO2 remains low (in the range from 0.03 to 0.08 cp [0.03 to 0.08 mPas]) despite its relatively high density (above 0.45 g/cm 3 ) under reservoir conditions. Thus, the viscosity of CO2 is lower by more than an order of magnitude than that of either crude oil or the brine occupying the remainder of the pore space of the reservoir rock. The resulting high mobility ratio leads to severe instability of the frontal region and significantly degrades the macroscopic efficiency of the displacement process. Some method of mobility control is required for efficient use of CO2 to increase greatly the quantity of producible oil. A promising approach to the goal of decreasing the mobility of CO2, well-explored in the laboratory and close to field trial, has been the use of foam. Such a composite fluid in which CO2 is used in conjunction with an aqueous surfactant solution is considerably less mobile in a porous medium than CO2 alone. The work was reviewed and some results were presented. 10 This work, however, pursues a different means to decrease the mobility of the CO2 displacement fluid. A direct thickener, a soluble polymer that sufficiently increases the viscosity of dense CO2, would be superior to a foam-like dispersion in two important respects that arise from the fact that a directly thickened CO2 could be injected without water. Therefore, there would be less trapped oil caused by increased water saturation, and a higher displacement efficiency could be attained. Furthermore, without injected water, problems resulting from corrosion would not be as severe as they have been in other CO2 projects. Although polymers are used in waterfloods to control mobility ratio, no data are available on similar use of such agents in CO2 floods. In fact, except for a preliminary report of this study, no search for viscosity-increasing polymers soluble in liquid or supercritical CO2 has been polymers soluble in liquid or supercritical CO2 has been reported in the literature. Francis has written two classic, general papers on solubility of simple organic and inorganic compounds in dense CO2. These give mutual solubilities of CO2 with more than 250 substances in various two- and three-component mixtures. Recently, Stahl et al. have described a method of microanalytical evaluation of the dissolving power of supercritical gases. Lundberg and Ali have been working on gas/polymer solutions at high temperatures and pressures. These researchers, however, seek low-viscosity solutions of polymers in dense gases like CO2, butane, propane, and ethane. SPEJ P. 679


1983 ◽  
Vol 23 (02) ◽  
pp. 281-291 ◽  
Author(s):  
Franklin M. Orr ◽  
Matthew K. Silva ◽  
Cheng-Li Lien

Orr Jr., Franklin M.; SPE; New Mexico Petroleum Recovery Research Center Petroleum Recovery Research Center Silva, Matthew K.; SPE; New Mexico Petroleum Recovery Research Center Petroleum Recovery Research Center Lien, Cheng-Li; SPE; New Mexico Petroleum Recovery Research Center Abstract Results of phase composition and density measurements for CO2/ crude-oil mixtures at 32C and four pressures are reported for a system in which liquid/liquid and liquid/liquid/vapor phase separations occur. The experiments demonstrate that a CO2-rich liquid phase can contain as much as 30 wt% hydrocarbons and show that a CO2-rich vapor phase at the same conditions extracts hydrocarbons less efficiently. Pseudoternary phase diagrams are presented that summarize the results of the detailed phase composition measurements. Results of slim-tube displacements at the same four pressures are also given. They indicate that displacement is efficient when the pressure is high enough that a liquid CO2-rich phase appears. Predictions of the performance of the slim-tube displacements based entirely on the performance of the slim-tube displacements based entirely on the experimental measurements of phase compositions and densities are obtained using a simple one-dimensional (1D) simulator. The simulation results clarify the roles of phase behavior and volume change on mixing in the slim-tube tests. Finally, the advantages and limitations of the slimtube and continuous multiple-contact (CMC) tests are compared. We conclude that the CMC experiment yields more information useful for prediction of the performance of a CO2 flood. Introduction The laboratory experiment most commonly performed in the evaluation Of CO2 flood candidates is the slim-tube displacement. The experiment is an attempt to isolate the effects of phase behavior on displacement efficiency in a flow setting that minimizes the effects of the viscous instability inherent in the displacement of oil by low-viscosity CO2. It provides useful information about the pressure required to produce high displacement efficiency in an ideal porous medium. It is not, however, a direct measurement of the phase behavior Of CO2/crude-oil mixtures. The physical behavior of such mixtures is usually studied by combining known quantities of oil and CO2 in a visual cell and measuring phase volumes at various pressures. The volumetric data obtained, along with saturation pressure pressures. The volumetric data obtained, along with saturation pressure data, do not give any direct evidence concerning displacement efficiency, but they can be used to adjust and tune representations of the phase behavior with an equation of state (EOS). For instance, Sigmund et al., used that procedure to match EOS calculations to PVT data and then simulated slimtube displacement experiments, obtaining good agreement between calculation and experiment. Gardner et al., used a combination of phase composition and volumetric measurements to construct ternary diagrams phase composition and volumetric measurements to construct ternary diagrams for a CO2/crude-oil system and then used the ternary diagrams in 1D simulations of slim-tube displacements. They also obtained good agreement between calculation and experiment. Thus there is at least some experimental confirmation of the relationship between equilibrium phase behavior and flow in an ideal porous medium. The connection between phase behavior and displacement efficiency has, of course, long been recognized. SPEJ p. 281


1968 ◽  
Vol 8 (04) ◽  
pp. 359-369 ◽  
Author(s):  
L.W. Holm

Abstract This study shows that in the presence of foam, gas and liquid flow separately through porous media representative of reservoir rock. These results were obtained by using tracer techniques to measure the flow of the gas and liquid comprising the foam. Foam does not flow through the porous medium as a body even when the liquid and gas are combined outside the system and injected as foam Instead the liquid and gas forming the foam separate as the foam films break and then re-form in the porous system. Liquid moves through the porous medium via the film network of the bubbles and gas moves progressively through the system by breaking and re-forming bubbles throughout the length of the flow path. The flow rates of the gas and liquid are a function of the number and strength of the films in the porous medium. There is no free flow of gas; i.e., no continuous gas phase. On the basis of these results, foam can be expected to improve a waterflood or gas drive by decreasing the permeability of the reservoir rock to a displacing liquid or gas. This improves the mobility ratio and thus the conformance of the flood. Introduction Foam is formed when gas and a solution of a surface active agent are injected into a porous medium either simultaneously or intermittently. During the past few years, several papers have been published on the subject of foam flow in porous media. Foam has been used successfully in the removal of capillary water blocks from producing formations. The use of foam in gas storage reservoirs to reduce gas leaks and to increase storage capacity has been considered in recent years. Foam has also been investigated as an oil displacing agent, and as an agent to improve the mobility ratio in a waterflood. However, the mechanism by which the gas and liquid phases comprising the foam flow through a porous medium has not been described adequately. Normally, when two immiscible phases (gas and liquid) flow concurrently through a porous medium, each phase follows separate paths or channels. At given saturations of the two phases, a certain number of channels are available to each phase, and as saturations change, the number and configuration of the channels available for each phase also change. The effective permeability of each phase is a function of the saturation of that phase only, and the flow of each phase can be described by Darcy's law. When foam is present, the effective permeability of the porous medium to each phase is greatly reduced compared with permeabilities measured in the absence of foam. Based upon the observed flow of surfactant solutions and gas in capillaries, it has been concluded that the gas and liquid may flow separately or they may flow combined as foam. At least four mechanisms have been postulated to explain how fluids flow with foam present:A large portion of the gas is trapped in the porous medium and a small fraction flows as free gas, following Darcy's law.The foam structure moves as a body; the rate of gas flow is the same as the rate of liquid flow.Gas flows as a discontinuous phase by breaking and re-forming films. Liquid flows as a free phase.A portion of the liquid and gas move as a foam body while excess surfactant solution moves as a free phase. It also has been suggested that different flow mechanisms exist for high quality (dry) foams made from dilute surfactant solutions and for foams made from more concentrated solutions. Studies conducted on the flow of foam through capillaries have shown that a plug-type flow occurs and that foam flows as a body.


Geofluids ◽  
2019 ◽  
Vol 2019 ◽  
pp. 1-12
Author(s):  
Zhuangzhuang Wang ◽  
Zhaomin Li ◽  
Hailong Chen ◽  
Fei Wang ◽  
Dawei Hou ◽  
...  

Foam is widely used as a selective blocking agent through mobility control in oil field development. Its flow behavior in porous media has been investigated sufficiently, but few studies were carried out to understand the change of foam texture in flow. In this work, sandpack and micromodel experiments were conducted simultaneously to analyze foam flow behavior from the perspective of foam texture. Based on the measured flowing pressure and the observed foam image, the correlation between blocking pressure and foam texture was quantitatively investigated. The blocking pressure has a strong correlation with average diameter (-0.906) and variation coefficient (-0.78) and has a positive correlation with the filling ratio (0.84). These indicate that the blocking performance of foam is influenced by its texture closely. But path analysis shows only that the average diameter and variation coefficient have a significant direct effect on blocking pressure (-0.624 and -0.404). These show that the blocking capacity of foam is mainly influenced by the size and uniformity of bubbles. Tiny, dense, and homogeneous foam has a stronger blocking capacity. This study provides a deep insight of foam flow in porous media.


SPE Journal ◽  
2007 ◽  
Vol 12 (02) ◽  
pp. 245-252 ◽  
Author(s):  
Dongxing Du ◽  
Pacelli Lidio Jose Zitha ◽  
Matthijs G.H. Uijttenhout

Summary Carbon dioxide (CO2) foam has been widely studied in connection with its application in enhanced oil recovery (EOR). This paper reports an experimental study concerning CO2 foam propagation in asurfactant-saturated Bentheim sandstone core and the subsequent liquid injection with the aid of X-ray computed tomography (CT). The experiments were carried out under various system backpressures. It is found that CO2 foam flows in a characteristic front-like manner in the transient stage and that the water saturation keeps at relatively high level at the outlet of the porous media because of CO2 solubility and capillary end effect. The subsequent surfactant solution injection shows a significant fingering behavior, accompanied by a low flow resistance over the core. It is also found that CO2 foam flow shows higher liquid saturation near the outlet and lower pressure drops under higher system backpressures. This can be attributed to the solubility of CO2 in the liquid phase. The results indicate the advantage of using foam in EOR processes such as water alternating foam (WAF), in which foam flow has higher sweep efficiency and stronger mobility control ability compared, for instance, to water alternating gas (WAG). Nevertheless, care should be taken during the water-injection stage in order not to favor the fingering. Introduction Foam applications in EOR and fluid (acid) diversion have grown considerably over the last three decades. For instance, WAGhas been regularly used in the field as a gasflood mobility control measure. Nevertheless, this technique has not always demonstrated the desired beneficial mobility effects because of the gravity segregation and the unstable preceding of the front between the water and moremobile gas (Holm 1987; Smith 1988). Creating foam by adding surfactant to the aqueous phase has proven to be able to increase the total recovery significantly by increasing the apparent viscosity of the system (Holm and Josendal 1974; Ali et al. 1985; Patzek 1996; Zhdanov et al. 1996; Turta and Signhal 1998). There are many attractive features of EOR using CO2 foaminjection. First, carbon dioxide is a proven solvent for reconnecting, mobilizing, and recovering waterflood residual oil. Many studies (Stalkup 1983) have shown that CO2 can achieve miscible-like displacement efficiency through multiple contacts (partitioning and extraction) with the crude oil. Second, CO2 is available naturally in large quantities and as a byproduct of lignite gasification and many manufacturing processes. Its price is also low, and there are no other large-volume uses competing for CO2. Third, with the push toward sustainable power production and the increasing realization for the need to reduce CO2 emissions, EOR using CO2 is becoming an important alternative for geological CO2 storage.


1984 ◽  
Vol 24 (02) ◽  
pp. 191-196 ◽  
Author(s):  
Stan E. Dellinger ◽  
John T. Patton ◽  
Stan T. Holbrook

Abstract As early as 1955, surfactants were recognized for their effectiveness in lowering gas mobility in reservoir cores by in-situ foam generation. For commercial field application a specific surfactant must have several important characteristics. it must behighly effective with low cost,chemically stable, soluble. and surface active in oil field brines, andunaffected by contact with crude oil or reservoir minerals. A static foam generator, an adaptation of a conventional blender, was used to screen more than 150 candidate surfactants. Promising additives were then ranked in a unique dynamic test, developed at New Mexico State U., that involves sequential liquid/gas flow in a vertical tube packed with glass beads. Conventional flow tests in tight, unconsolidated sandpacks show good correlation with the dynamic and static screening tests, especially those data obtained in the dynamic experiment. Some synergism exists between additives with amine oxides and amides having the most beneficial effect on foam stability and gas mobility control. The utility of cosurfactant stabilization was demonstrated in linear, two-phase flow tests through tight. unconsolidated sandpacks involving brine and gas. A solution containing 0.45% Alipal CD-128 (TM) and 0.05% Monamid 150-AD (TM) can decrease gas mobility over 100-fold. The effect appears to be time-independent, indicative of good foam stability. Alipal CD-128 alone reduces gas mobility even more, usually by a factor of two. The moderating influence of a cosurfactant could be beneficial in avoiding "overcontrol" of mobility, especially in low-permeability reservoirs. Introduction For more than 30 years recovery experts have known that CO2 possesses a unique ability to displace crude oil from reservoir rock. Although many gases have been tested for their crude-displacing efficacy, only CO2 has the ability to reduce residual oil saturations to near zero and produce significant quantities of tertiary oil in models that have been previously waterflooded to the economic limit. Early studies provided the fundamental understanding required to explain the high efficiency of CO2, but until recently the depressed price of crude has made most, if not all, CO2 field applications unprofitable. A common failing among-as-driven oil recovery processes is the severe gas channeling that occurs in the reservoir because of excessively high gas mobility. Optimistic oil recoveries obtained in laboratory flow tests with small-diameter, linear models have never been achieved in the field. Both miscible and immiscible drive processes suffer because gas channeling causes most of the oil reservoir to be bypassed and the oil left behind. The earliest work relative to the problem of lowering the mobility of CO2 does not involve CO2 at all. Because of the high potential for miscible drives that use enriched gas mixtures, considerable study was undertaken in the late 1950's on techniques to mitigate gas channeling. A few visionary investigators considered the use of foams as a possible solution to the problem. The earliest reported work was conducted by Bond and Holbrook, whose 1958 patent describes the use of foams in gas-drive processes. Because of the high cost of CO2 relative to crude oil during this period, CO2 processes were ignored. The use of foams in conjunction with CO2, was not contemplated until much later when rising crude prices revived interest in the CO2 displacement technique. CO2 exists as a dense gas or supercritical phase under reservoir conditions: therefore, experiments on controlling gas mobility are usually applicable to CO2 even though they may have been conducted with other gases such as nitrogen, methane, or even air. Concurrent with Bond and Holbrook's work, Fried, working at the USBM laboratory in San Francisco, demonstrated the potential of foam to lower the mobility of an injected gas phase. Fried's work was followed by some excellent work reporting an experimental technique involving in-situ foam generation promoted by injecting alternate slugs of surfactant solution and gas. Their patent related to the use of foam for mobility control in CO2 injection processes is especially pertinent. Laboratory work was encouraging enough that Union Oil Co. conducted a field test in the Siggins field, IL. Foam generation by alternate-slug injection and simultaneous gas-solution injection was tested. This test indicated that at concentrations below 1% the foaming agent, a modified ammonium lauryl sulfate, did not produce an effective foam. Above 1%, reduced gas mobility was obtained; however, at least 0.06 PV of surfactant solution had to be injected to achieve lasting mobility control. Since the tests were conducted sequentially, with the higher concentrations injected last, it is possible that the required amount of surfactant may be understated. A 0.1-PV bank might be more realistic for lasting mobility control. Their results also indicated that adsorption may reduce the effectiveness of a surfactant. It was suggested that future tests might benefit by selection of agents that are less strongly absorbed than ammonium lauryl sulfate. SPEJ P. 191^


1977 ◽  
Vol 17 (05) ◽  
pp. 358-368 ◽  
Author(s):  
Mahmoud K. Dabbous

Abstract Injection of polymers in advance of a micellar fluid slug has been considered to improve reservoir volumetric sweep in a tertiary-mode micellar flood. An investigation was made of the injection of polyacrylamide-type polymers in waterflooded polyacrylamide-type polymers in waterflooded porous media and its effects on a subsequent porous media and its effects on a subsequent micellar flood. It was found that the presence of waterflood residual oil saturations in the porous medium increased the flow resistance and residual resistance factors (2- to 3.5-fold) compared with their corresponding values when the rock was free of residual oil. Inaccessible pore volume to polymer flow also appeared to be larger when waterflood residual oil saturations were present. These effects have been attributed to wettability and phase distribution of fluids in the porous medium. phase distribution of fluids in the porous medium. The study emphasized basic differences in the flow behavior of polymer injected ahead of a micellar slug (to improve sweep) and behind the micellar fluid (to control mobility). Both effects are for improved oil-recovery efficiency. Water mobility was greatly reduced following the displacement of polyacrylamide polymers in the waterflooded cores, yet mobility of the oil-water bank in a subsequent micellar flood was reduced to a lesser degree than the water bank. For a residual resistance factor to water ranging from 2 to 7, mobility control of a subsequent micellar flood could be achieved with a 22- to 39-percent increase in polymer concentration in the mobility buffer bank. This increase is in excess of the concentration required for a flood not preceded with polymer injection. Polymer preinjection had no adverse effects on oil displacement characteristics of the micellar fluid and appeared to reduce surfactant adsorption on the rock for the polymer-micellar system studied. Some experimental data indicated that the oil bank breaks through earlier and at a slightly higher oil cut in linear core floods. Such a result is theoretically feasible if the reduced-mobility water is not completely displaced at the front end (immiscible portion) of the oil-water bank. Oil-bank breakthrough probably would be delayed in the reservoir because of the action of the preinjected polymer to decrease the flow of fluids in polymer to decrease the flow of fluids in high-permeability zones. Introduction In a previous paper, preinjection of polymers in advance of a micellar slug was proposed as a means for improving reservoir volumetric sweep and oil recovery by a micellar flood. Increased flooding efficiency should result from reduced interwell permeability contrast in the reservoir following the polymer treatment. Preinjection of polymers also should result in better preflushing polymers also should result in better preflushing efficiency in displacing incompatible formation brines over "conventional" water preflushes. Thus, an improved oil-recovery method designed to increase reservoir volumetric sweep and miscibly recover tertiary oil consists ofpreinjection of a carefully designed slug of preinjection of a carefully designed slug of high-molecular-weight polyacrylamide polymers followed by a water-bank spacer to displace the polymer in the interwell area, andinjection of polymer in the interwell area, andinjection of a surfactant (micellar) slug followed by a polymer mobility buffer bank and chase water. The fluid banks that are injected or developed during the process are illustrated in Fig. 1. Mixing and process are illustrated in Fig. 1. Mixing and interaction zones at fluid-bank boundaries are not shown in the schematic. The preinjection of a polymer is intended to rectify interwell permeability variation. The polymer is injected in reservoir rock that has waterflood residual oil saturations. SPEJ p. 358


1981 ◽  
Vol 21 (05) ◽  
pp. 603-612 ◽  
Author(s):  
C.S. Chiou ◽  
G.E. Kellerhals

Abstract For the surfactant formulations used (particular surfactant concentration, surfactant type, cosolvent type, cosolvent concentration, etc.), the results show that surfactant systems containing polymer as a mobility control agent may exhibit adverse polymer transport behavior during flow through porous media. Polymer generally lagged behind the surfactant even though the two species were injected simultaneously in the surfactant slug. This poor polymer transport definitely could have a detrimental effect on the efficiency of a micellar flooding process in the field. Phase studies show that when some surfactant systems containing xanthan gum are mixed with crude oil at various salinities, a polymer-rich, gel-like phase forms. The polymer lag phenomenon in core tests can be related to phase separation due to divalent cations generated in situ as a result of ion exchange with the clays and the surfactant. Introduction and Background Proper design for mobility control is important in micellar or surfactant flooding to maintain stable displacement and prevent or reduce viscous fingering. Generally, effective mobility control is obtained by having the mobility of the polymer drive less than the mobility of the surfactant slug and the mobility of the surfactant slug less than the mobility of the oil/water bank. Oil-external and aqueous surfactant systems are designed to attain mobility control by two distinct approaches. In the oil-external case, increases in viscosity (compared with water) are largely a result of the presence of oil and the relatively high concentration of surfactant in the slug. The viscosity of aqueous surfactant systems frequently is increased by the addition of a polymer, usually either xanthan gum or polyacrylamide. There are drawbacks to both of these approaches. Use of a hydrocarbon such as crude oil (in the surfactant slug) to increase viscosity may result in injectivity problems due to wax and/or asphaltenes in the crude oil.Trushenski investigated the effects of sulfonate, cosurfacant, water, and salt concentrations on sulfonate/polymer incompatibility (multiple phases may form when polymer solution dilutes with a sulfonate containing micellar fluid). In dynamic core tests, this phase separation may result in one phase being trapped in the porous media. For the sulfonate/cosurfactant system (Mahogany AA and isopropyl alcohol) used, the results of static phase studies correlated with the incidence of phase trapping in dynamic core tests. Trushenski concluded that increasing the concentration of cosurfactant or cosolvent in the surfactant and polymer slugs could eliminate or reduce sulfonate/polymer incompatibility. In his dynamic core tests, the absolute brine permeability of the Berea cores was characteristically about 500 md. Polymer type (polyacrylamide or polysaccharide) did not appear to affect phase behavior appreciably. He identified sulfonate/polymer incompatibility as a previously unreported source of sulfonate loss. Trushenski also concluded that invasion of a surfactant slug by a water-soluble polymer can be eliminated or minimized if the surfactant slug contains low concentrations of crude oil.Pope et al. studied the phase behavior of surfactant/brine/alcohol systems both with and without polymer. Some of their various combinations also were equilibrated with a synthetic oil consisting of n-octane or an n-octane/benzene mixture. Both anionic and nonionic polymers were used. At a sufficiently high sodium chloride concentration, the oil-free (no added oil) mixtures showed phase separation into an aqueous polymer-rich phase and an aqueous surfactant-rich phase. They termed the salinity at which phase separation occurred the critical electrolyte concentration. SPEJ P. 603^


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