|Publication number||US2846012 A|
|Publication date||Aug 5, 1958|
|Filing date||Dec 6, 1954|
|Priority date||Dec 6, 1954|
|Publication number||US 2846012 A, US 2846012A, US-A-2846012, US2846012 A, US2846012A|
|Inventors||Roy H Lorenz, Orrin C Holbrook, George G Bernard|
|Original Assignee||Pure Oil Co|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (2), Referenced by (9), Classifications (10)|
|External Links: USPTO, USPTO Assignment, Espacenet|
I p I 2,846,012. RE OVERY-Ol on; FROM PARTIALLY DEPLETED RESERVOIRS BY SECONDARY, RECOVERY Roy H. Lorenz; Arlington Heights, and ommclnoibrook and George G. Bernard, Crystal Lake,'lll;, as-
signors to The Pure Oil Company, Chicago, Ill., a corporation of Illinois A pp lication' Dece mber 6,
"Serial No. 473,473 y i ,9, Claims. 01. l66-v-38) invention .is concerned with increasing" the efl'iciencyof secondary recovery methods employed in producingpetroleumsoil from 'partially' depleted subterranean reservoirs.
It more specifically relates to modifying the Wettability of a" formation reservoir in controllingthe movement'of a water injection fluid through the openings of an oil-containing reservoir. I
The phenomena of capillarity and surface tension and their application in. petroleum production have been extensivelyi studied. It is wellknown that these phenomena influence the efliciency of processes "employed in the production of=petroleum oils from subterranean'r'eservoirs l atented Aug. 5
controlling the wetting characteristics of the injection fluid. From a'wettability standpoint, formations are encounteredwhich are oil-wet, or water-wet. Whileimoet reservoirs'are considered preferentiallyWater-wet, it 15 possible to have reservoirswhich are intermediate in wettability, being on a borderline between oil-wet and water wet. A number of procedures have been used to change the characteristics of the formation from water-wet to oil-wet in order to avoid the loss in mobility'of a, fluid which will wet the formation reservoir surfaces and thereby adhere thereto. Ina water-wetformationthe water is distributed in the finer capillaries, and ina more orless thin layer over the entire surface accessible to fluid contact. Because the water is restricted tothe smaller interstitial passageways and'is spread out. over a large solid surface, its mobility is not .as great as that of the oil 1 which is located in the larger interstitial passageways and b -called Secondary recovery methods wherein the,
residual oil is flushed or driven from therock reservoir bysinjectinginto the reservoir by means of an injection well vadrive fluid such as water or gas. 'Theproduced fluidsiare recovered for further processing by means ofa recovery well or wells. In facilitatingthe use of water asf 'a drive fluidin the treatment of oil sands, a number of expedients have been'employed to complement the effect of.--the diive fluid. 1 Surface-active agents have'fbe'e'niused to induce the preferential wetting of the sand by the water'flood rather than by the r'eser'voiroilin order to permit the oil 'to bemore readily driven out by thewaterflooding. However, itis an object of the instant invention,
to employ the opposite approach and facilitate reservoir drainage in secondary recovery operations by makin gthe formation preferentially oil-wettable in a' peripheral zone immediately adjacent the well bore. This and other obje'cts will become more apparent from the followingde' tailed description of the instant invention' I In-the water flooding of depleted or' partially dc-i pleted subterranean oil-bearing'reservoirs to recover the] residual oil, the initial flow of water into the formation openings is controlled by a number'offactors. From a' geometrical standpoint, considerableflow'resistance is encountered due to the limited access p'r'o'videdby the is spread out over a water surface. ,Thus if the water -is to move it must overcome the resistance ofthe solid-' water interface and the oil-water'interface, while the oil has only to overcome the resistance offered by the"oil-. water interface. Furthermore, the oil, occupying the larger interstitial passageways, has larger channels available to flow through than does the water. From this .it is evident that if two fluids are present in a rock, the
. non-wetting fluidsh'ould fi nd less resistance to flow.
In water injection wells two fluids, oil and wa ter, are present in the surrounding formation. After a relatively short injection period, most .of'the .recoverableoil will have been "flushed from the area immediately surrounding the well bore to a radius of about 10-20 feet. 'If the formation is water-wet, as is the more common case, the
Water passing through the flooded-out section of '10 feet" radius will meet the resistance toflow" of a water-wet 'system which is-higher than would be the caseof an oil- 1 I wet system. Therefore, according to this' invention the introduction of water'into a partially depleted oil-bearing. reservoir is facilitated by modifying jfthe. characteristicsv small amount of area of rock face which is exposed by I a traversing bore hole of relatively small diameter. Limitations in the size of the formation openings directly entering; into the borehole can be overcomeby the use of formation penetrators, such is to increase the size of the interstitial openings which channel out in a'radial, horizontal direction from the borehole, thereby increasing the porosity and permeability of the formation in an area near the "bore hole. I The use of these expedien'ts involves specialequipment, the use of which can greatly add to the expe'nse entailed in.
' producing oil fromjs'ubterranean reservoirs. These tech-- niques improve'the fluid distribution by increasing the sizefof theinterstitial openings; thereby reducing the resistancetothe flow of fluid'stherethrough. The fluid distribution can alsobe influenced by-modifying the etfecr tive permeability characteristics of the formation withoutin'j fact increasing the diameter of the interstitial, openas acidizing media of hydraulic fracturing fluids. The function of thesepr'ocesses change in effective .permeability is effected by of this substantially oil-free, circumambient zone immediately adjacent the borehole, which is serving as the injec tion well, to make the formation'surfaces in this 1mg preferentially oil-Wettable. Thischange in wettability -is effected in the instant; invention by coating the 'forfn'a tion surfaces in this circumambient zonewith a mono.
molecular silicone coating. In the' prior art, a number of expedients have been described-fortreating forma-, tions with silicones. In U. "S. Patents 2,4 69,354and, 2,633,9l9 silicone coatings have been provided on the formation reservoir surfaces by treatingthe formation with a silicon halide,'.such as methyl dichlorosilane, which I is subsequently hydrolyzed to form a silicone polymer which is adsorbed on the surfacesof theformation. "In, employing [silicon halides it is necessary that the formai tion befdried by the use of heating and/ or solvent washa, ing in order to prepare the reservoirsurfaces prepara-, tory to coating the'mjwith the silicone polymer. ,Su ch preliminary treatment requires the use of auxiliary, equipment and frequently, in spite of the efliciencyofthis equipment, complete drying is not always effected, which influences the eflicacy of'the treat. In U. S. Patent 2,614,635 this disadvantage isovercome in thetreating of subterranean formations by employing an .oillsolution containing a small amount ofa liquid. silicone lpoly mer, To be effective, the silicone solution mustbeheated to a temperature of at least about1500 F, While, inthisQ instance, it is unnecessary. to employ a dehydratingstegl;
3 conducted economically it is necessary that this oil, or at least a substantial amount of it, be recovereved. This, however, is not always possible because the irreducible minimum saturation of formation areas with this oil may occur, preventing its recovery. In practicing the instant invention these disadvantages are overcome by the use of water-soluble salts of esters of siliconic acids as the silicone-forming agents. Such materials, because of their water-solubility, may be readily introduced directly into the water flood and injected into the formation whereby a silicone coating is formed on the reservoir surfaces without the need for dehydrating the formation or using oil solutions of silicone-forming agents. The, siliconeforming substances which may be employed in the instant invention are those water-soluble salts of esters of siliconic acid which decompose and precipitate a silicone when contacted with a weakly acidic solution. Examples of suitable siliconates for use in carrying out the invention include the water-soluble alkyl, aryl, and alkaryl derivatives of the siliconic acid salts or mixtures thereof. Specific metal siliconates include sodium methyl siliconate, potassium ethyl siliconate, calcium phenyl siliconate, barium benzyl siliconate, lithium propyl siliconate. Although only alkali metal and alkaline earth metal siliconates are specifically illustrated, other cationic substituents may be employed.
Other suitable salts include aluminum, zinc, copper, etc.,
as Well as the substituted ammonia salts. The preferred salts are the alkali metal and substituted ammonia salts because of their excellent water-solubility which prevents any deleterious precipitates from forming within the formation due to the presence of cations which may react to form waterand oil-insoluble products. The siliconic acids which are utilized in preparing the salts of this invention maybe formed by hydrolyzing alkyl trichlorosilanes to form a hydrolyzate which then is neutralized with aqueous sodium hydroxide according to conventional neutralization techniques. Methods of preparing metal organic siliconates are described in detail in U. S. Patents 2,438,055, 2,441,422, and 2,441,423. If alkyl siliconates are dried, free-flowing water-soluble powders can be produced. One suitable water-soluble alkyl siliconate, sodium methyl siliconate, is commercially available and may be purchased from the General Electric Company under the mark SC-50.
In employing the silicone-forming solutions of this invention, dilute solutions of the metal organic siliconate are employed. Satisfactory results can be obtained using solutions containing .01 to 10% of the silicone-forming agents of this invention, although amounts outside this range may be employed. The siliconate is introduced directly into the flood water and pumped into the subterranean reservoir. The siliconate solution is then contacted Within the formation interstices with an acidic solution. On mixing, the siliconate reacts with the acid to form a silicone polymer which coats the sand surface and makes it preferentially oil-wettable. Solutions of acids, especially weak acids such as carbon dioxide, phenol, acetic acid, low concentrations of hydrochloric acid and nitric acid, etc., are especially suitable for producing silicone polymer coatings.
In the practice of the instant invention a water injection well, having a ten ft. thick injection zone, is treated using conventional flooding apparatus by adding sodium methyl siliconate to the injection water at the well head in sufficient amount. to provide approximately 10,000 gals. This volume is sufficient to fill half of the pore volume within a 20 ft. radius of the well bore with a 0.5% solution of sodium methyl siliconate. After all of this solution has been injected into the well (in the course of normal water injection operations), the injection of 10,000 gals. of an aqueous 5% HCl solution is started (after first flushing the sodium methyl siliconate solution from the well bore with water). After the HCl injection, normal water injection is again started. As the H01 I formation care must be taken in the selection of the acidic reagent employed to avoid using an acidic substance that would spend itself by reacting with the. formation constituents and become ineffective. For example, hydrochloric acid should not be employed in treating calcareous formations. The amount of siliconate solution which is initially introduced into the formation will depend, of course, upon the extent and structural characteristics of the formation. Porosity, which may be readily determined by standard procedures (Vide Elements of Oil Reservoir Engineering, Pirson, McGraw-I-Iill, 1950 at p. 20 et seq.), is a convenient criterion. Accordingly, a volume of siliconate solution equal to 25 to 75% of the pore volume of a circumambient section of formation having a radius of about l0-20 feet should be used, and preferably about 50% of said pore volume. Amounts outside this range may also be employed. However, maximum benefits are obtained by facilitating the flow through that section of formation adjacent to the injection well bore. In forming the silicone coating the amount of acidic reagent which is introduced into. the formation will depend upon the amount of siliconate which is employed because the neutralization reaction proceeds stoichiometrically and requires an equivalent amount of acid solution. In order to insure complete precipitation of the silicone coating an amount of acidic reagent in excess of the stoichiometric amount should be used.
Thus, by treating a circumambient section of the oilcontaining reservoir in order to make it oil-wet by means of the invention, the resistance to water flow is lowered, thereby decreasing the pumping cost and expediting the water flood. Conventional water-flooding equipment can be employed without substantial modification. No significant amounts of oil are lost because the section treated has already been water flooded and no additional amounts of oil are introduced into the formation.
Therefore, We claim as our invention:
1. In a secondary recovery process employing a water drive to facilitate the drainage of residual petroleum oil from a partially depleted, subterranean oil-bearing normally water-wettable reservoir, traversed by a water injection well. and a recovery well, a method for minimizing the resistance of said reservoir to the flow of said water drive through a circumambient zone immediately adjacent said injection well which comprise forcing into said reservoir through said injection well an aqueous solution conta'ining about 0.1-l0% by weight of a water-soluble metal salt of an organic siliconic acid into a circumambient zone immediately adjacent the injection bore hole and. having a radius not greater than about 20 feet, in a volume equal to about 25-75% of said zone, contacting the aqueous salt-containing solution While in said circumambient zone with an acidic solution whereby a silicone polymer is precipitated to form an oil-Wettable coating on the mineral surfaces of said circumambient zone without deleteriously affecting the specific permeability of said zone, and injecting a water injection fluid into said reservoir through said zone to force said residual oil therefrom.
2. In a secondary recovery process employing a water drive to facilitate the drainage of residual petroleum oil from a partially depleted, subterranean oil-bearing normally water-wettable reservoir, traversed by a water injection well and a recovery well, a method for minimizing the resistance of said reservoir to the flow of said water drive through a circumambient zone immediately adjacent said injection well which comprise forcing into said reservoir through said injection well an aqueous solution con- 7 salt of an organic siliconic acid intoa circumambient zone immediately'adjacent the injection bore hole and having a radius Within the range of about 10-20 feet, in a volume equal to about 25-75% of the pore volume of said zone, contacting the aqueous salt-containing solution while in said circumambient zone with an acidic solution whereby 'salt is an alkali metal alkyl siliconate.
4. A method in accordance with claim 3 in which the siliconate is sodium methyl siliconate.
5. A method in accordance with claim 2 in which the acidic solution is a solution of a weak acid selected from 'the group consisting of aqueous solutions of carbon dioxide, phenol, and acetic acid.
6. A method for recovering oil from partially depleted normally water-wettable oil-containing subterranean formationby employing a water injection well and a recovery well, which comprises introducing a first water injection fluid from said injection well into said formation until a circumambient zone having a radius not greater than about 20 feet adjacent the water injection well is substantially free of oil, introducing into the injection water 0.01l0% by weight of a water-soluble metal salt of an organic siliconic acid, forcing the salt-containing water in a volume equal to about 25-75% of the pore volume of said circumambient zone into said formation, contacting the salt-containing injection water while in said circumambient zone with an acidic solution whereby a silicone polymer is precipitated to form an oil-wettable'coating on the mineral surfaces-of said circumambient zone, Without deleteriously afiecting the specific permeability of said zone, and thereafter continuing the injection of said first, water injection fluid into said formation' 7. A method in accordance with claim 6 in which the salt is an alkali metal alkyl siliconate.
8. A method in accordance with claim 7 in which the siliconate is sodium methyl siliconate.
9. A method in accordance with claim 6 in which the acidic solution is a solution of a weak acid.
References Cited in the file of this patent 1 V UNITED STATES PATENTS MacMullen Mar. 4, 1952
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US2587636 *||Dec 31, 1948||Mar 4, 1952||Cowles Chem Co||Method of making alkali metal salts of organosiloxanols and organosilanetriols|
|US2633919 *||Jun 19, 1948||Apr 7, 1953||Union Oil Co||Treatment of oil-bearing formations|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US3036630 *||Jan 9, 1961||May 29, 1962||Pure Oil Co||Water-flood process for claycontaining formation|
|US3087542 *||Dec 2, 1958||Apr 30, 1963||Gulf Research Development Co||Process for plugging formations|
|US3123139 *||Feb 16, 1961||Mar 3, 1964||rs to Continental Oil Cosiiisany||Oil well waterfjlooding|
|US3286770 *||May 25, 1965||Nov 22, 1966||Halliburton Co||Method of treating wells|
|US3498378 *||Jun 9, 1967||Mar 3, 1970||Exxon Production Research Co||Oil recovery from fractured matrix reservoirs|
|US4197912 *||Dec 21, 1978||Apr 15, 1980||John C. Thompson||Oil recovery via silicone introduction|
|US4479543 *||Jul 28, 1983||Oct 30, 1984||Union Oil Company Of California||Method for deeper penetrating acidizing of siliceous formations|
|US4787453 *||Oct 30, 1986||Nov 29, 1988||Union Oil Company Of California||Permeability stabilization in subterranean formations containing particulate matter|
|US4957639 *||Jun 1, 1987||Sep 18, 1990||Emox High Technology, Inc.||Method for enhancing recovery of oil and compositions related thereto|
|U.S. Classification||166/270, 556/463, 507/264, 507/936, 507/234, 507/267|
|Cooperative Classification||C09K8/86, Y10S507/936|