Direct Thickeners for Mobility Control of CO2 Floods

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

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


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^


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


Author(s):  
Sultan Ayoub Meo ◽  
Abdulelah Adnan Abukhalaf ◽  
Omar Mohammed Alessa ◽  
Abdulrahman Saad Alarifi ◽  
Waqas Sami ◽  
...  

In recent decades, environmental pollution has become a significant international public problem in developing and developed nations. Various regions of the USA are experiencing illnesses related to environmental pollution. This study aims to investigate the association of four environmental pollutants, including particulate matter (PM2.5), carbon monoxide (CO), Nitrogen dioxide (NO2), and Ozone (O3), with daily cases and deaths resulting from SARS-CoV-2 infection in five regions of the USA, Los Angeles, New Mexico, New York, Ohio, and Florida. The daily basis concentrations of PM2.5, CO, NO2, and O3 were documented from two metrological websites. Data were obtained from the date of the appearance of the first case of (SARS-CoV-2) in the five regions of the USA from 13 March to 31 December 2020. Regionally (Los Angeles, New Mexico, New York, Ohio, and Florida), the number of cases and deaths increased significantly along with increasing levels of PM2.5, CO, NO2 and O3 (p < 0.05), respectively. The Poisson regression results further depicted that, for each 1 unit increase in PM2.5, CO, NO2 and O3 levels, the number of SARS-CoV-2 infections significantly increased by 0.1%, 14.8%, 1.1%, and 0.1%, respectively; for each 1 unit increase in CO, NO2, and O3 levels, the number of deaths significantly increased by 4.2%, 3.4%, and 1.5%, respectively. These empirical estimates demonstrate an association between the environmental pollutants PM2.5, CO, NO2, and O3 and SARS-CoV-2 infections, showing that they contribute to the incidence of daily cases and daily deaths in the five different regions of the USA. These findings can inform health policy decisions about combatting the COVID-19 pandemic outbreak in these USA regions and internationally by supporting a reduction in environmental pollution.


Author(s):  

Abstract A new distribution map is provided for Chrysomyxa arctostaphyli Dietel Fungi: Basidiomycota: Uredinales Hosts: Picea spp. and Arctostaphylos uva-ursi. Information is given on the geographical distribution in NORTH AMERICA, Canada, Alberta, British Columbia, Manitoba, New Brunswick, Newfoundland, Northwest, Territories, Nova Scotia, Ontario, Quebec, Saskatchewan, Yukon, USA, Alaska, Arizona, Colorado, Idaho, Maine, Michigan, Montana, New Mexico, New York, Oregon, South Dakota, Utah, Washington, Wisconsin, Wyoming.


Author(s):  

Abstract A new distribution map is provided for Xylella fastidiosa Wells et al. Gammaproteobacteria: Xanthomonadales: Xanthomonadaceae. Hosts: many. Information is given on the geographical distribution in Europe (Italy), Asia (Iran and Taiwan), North America (Canada, British Columbia, Ontario, Saskatchewan, USA, Alabama, Arizona, Arkansas, California, Delaware, Dstrict of Columbia, Florida, Georgia, Indiana, Kentucky, Louisiana, Maryland, Mississippi, Missouri, New Jersey, New Mexico, New York, North Carolina, Oklahoma, Oregon, Pennsylvania, South Carolina, Tennessee, Texas, Virginia, Washington and West Virginia), Central America and Caribbean (Costa Rica and Puerto Rico) and South America (Argentina, Brazil, Bahia, Espirito Santo, Goias, Minas Gerais, Para, Parana, Rio de Janeiro, Rio Grande do Sul, Santa Catarina, Sao Paulo, Sergipe, Paraguay and Venezuela).


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