GELLING AQUEOUS SILICATE COMPOSITIONS

Abstract: An aqueous silicate solution is solidified using a thermally responsive gelation activator which is a reducing sugar selected from lactose, dextrose, fructose, galactose, mannose, maltose, xylose and mixtures thereof. The aqueous silicate solidification method can be utilized for sealing a subterranean formation.

Description: This invention relates to a method of gelling aqueous silicate-containing compositions. In the production of fluids from a permeable subterranean formation, it is often helpful and sometimes necessary to reduce the permeability of portions or zones of the formation. This entails sealing or plugging certain interstitial spaces, channels, fissures, and the like in order to seal off, plug, or otherwise obstruct openings providing fluid passageways in the permeable for­ mation penetrated by a well bore. Aqueous sliliate solutions which are gelled or solidified with acid producing activators have been known and used in many applications including sealing and consolidation processes carried out in subterranean for­ mations. A number of water-soluble silicates and processes using such silicates are disclosed in our U.S.-A-3202214 and 3,435,899, to which reference should be made for details. Sodium silicate is a complicated system of various molecular weight silica polymers in an alkaline solution. Aside from requiring a certain minimum amount of alkalinity, sodium silicate has no definite chemical combining numbers. When sodium silicate is acidified to a pH less than about 10 or 11, the sodium silicate is converted partially to silicic acid. Silicic acid exists at these alkaline pH's as a weak acid. Instead of precipitating and producing silica, SiO₂, the silicic acid remains hydrated and forms a three-dimensional network entrapping the solvent water. This network is a gel since both phases are continuous. A slight lowering of the pH brings about radical changes in gel time. Consequently, gel times are difficult to control, and lumping from local acid concentrations during large scale mixing frequently occurs. Sodium silicate may be caused to form a gel which will seal an underground formation or plug capillaries therein by the addition of polyvalent cations such as Ca⁺⁺, Fe⁺⁺⁺, Cr⁺⁺⁺, Cu⁺⁺, etc. However, the addition of the polyvalent cations described above utilizing salts containing the cations may cause immediate gelation of the sodium silicate which allows no time to pump the solution into the formation. U.S.-A-3,202,214 discloses a method of gelling an aqueous silicate composition utilizing a reducing agent and an oxidizing agent. Although the method described therein is useful in many applica­ tion, the use of oxidizing and reducing agents to gel an aqueous sodium silicate-containing com­ position results in increased expense and the gel produced therefrom undergoes syneresis and is thus not totally satisfactory for use in treating a sub­ terranean formation. Furthermore, the gels formed by the use of an oxidizing agent and reducing agent are not particularly effective in treating sub­ terranean formations having temperatures between 120°F and 170°F (49°C and 77°C). The present invention provides a method of gelling aqueous silicate compositions through the use of thermally responsive gelation activators, which overcomes or at least mitigates the above described problems. By the present invention, thermally responsive silicate gelation activators are utilized which can be mixed with an aqueous silicate solution as part or all of the required acid producing activator; yet, the composition containing the activator has a reduced gel rate until the temperature of the mix­ ture is raised to a given level, which is at least 120°F (49°C). The use of such thermally responsive aqueous silicate compositions makes it possible to apply or place the compositions in particular applications with little or no risk of premature gelation. Furthermore, the aqueous silicate-­ containing compositions of this invention can be prepared in advance and stored for relatively long periods of time, such as 24 hours, before use. Silicates which can be used for the composi­ tions and methods of this invention are water-­ soluble silicates which form silicate polymer chains or gel upon acidification. The preferred silicates are those of alkali metals, especially sodium, potassium and mixtures thereof. These silicates are commercially available as dry powders or concentrated aqueous solutions having from about 31 to about 55 parts solid per 100 parts of solu­ tion and a pH of in the range of from about 10 to about 13.5 (hereinafter referred to as "concentrated aqueous silicate"). The concentrated aqueous sili­ cate and the aqueous silicate mixtures of the pre­ sent invention including the temperature responsive activators described hereinafter preferably have a pH greater than about 9, most preferably in the range of from about 10 to about 13 at temperature levels below the activation temperature period. Upon activation and the production of acid or acid equivalents by the activator, the pH of the aqueous silicate mixture is decreased to a pH below about 9 and the mixture gels or sets. The delay and long shelf life referred to herein is the time period following mixing of a temperature responsive acti­ vator of the present invention with an aqueous silicate solution and ending with the beginning of gelation and does not refer to the actual gelation period. Preferably, the water-soluble silicates, that are employed in the present invention have a molar ratio of silicon dioxide to alkali metal oxide in the range of from about 0.5 to 1 to about 3.5 to 1 and the alkali metal is sodium, potassium, and mix­ tures thereof. The preparation of these silicates is well known in the art and is disclosed in U.S. Patent 4,525,285, which is assigned to the assignee of the present invention and is hereby incorporated by reference. The thermally responsive gelation activators of the present invention can generally be described as reducing sugars. Example of suitable reducing sugars include lactose, dextrose, fructose, galac­ tose, mannose, maltose, and xylose. The preferred reducing sugar for use in the present invention is lactose. In general, the reducing sugars may be incor­ porated into the aqueous silicate solutions either as an anhydrous solid or as an aqueous solution, both of which forms are commercially available. Generally, from about 10 to about 300 percent by weight of reducing sugar based on the amount of silicate present in the aqueous silicate solution may be employed in gelation of the aqueous silicate solution. It will be appreciated, however, that the amounts of reducing sugar utilized will vary widely depending on the formation to be treated and the desired gelling rate. In addition to the aqueous silicate solutions which contain the silicate and reducing sugar, a reactive salt capable of reacting with the alkali metal silicate may be included therein. For example, when a reactive salt is employed in the aqueous silicate solutions which contain the sili­ cate and reducing sugar, the amount of reducing sugar employed is reduced and the gelling rate of the silicate solutions is increased which results in improved economics in carrying out the present invention. Preferably, a reactive salt is not uti­ lized in formations having a temperature greater than 120°F (49°C). The term "reactive salt" is intended to mean those Group I - Group II metal salts which chemically react with the aqueous silicate to pro­ duce a completely or substantially water-insoluble gel. Specific reactive salts include calcium chloride, magnesium chloride, potassium chloride, sodium chloride, and mixtures thereof. The pre­ ferred reactive salt is calcium chloride. When a reactive salt is utilized in the aqueous silicate solutions, it is generally incorporated into the aqueous silicate solution in an amount to produce a concentration of salt in the range of from about 0.5 g/liter to about 5 g/liter of solution. Of course, the amount of reactive salt employed should be insufficient to immediately form a satisfactory gel if used alone with the silicate. Care should be taken not to use highly excessive amounts of reactive salts of polyvalent metals since such reactive salts can readily form insoluble complexes with the silicate which then will precipitate from the system. The compositions of the invention will incor­ porate sufficient water to render them fluid. Generally, at least a portion of the necessary water will be supplied by using a commercial aqueous silicate solution, as described above, with additional water being supplied, if desired, or by the admixture of water and reducing sugar and/ or by any reactive salt solution when employed. It will be appreciated that amounts of ther­ mally responsive silicate gelation activator, added water, and, when utilized, reactive salt used in proportion to the silicate, as well as the quan­ tity utilized in treating a subterranean formation, varies widely depending on the temperature, poro­ sity, permeability and other factors of the for­ mation. Accordingly, it generally is not feasible to define, in terms of proportions, a silicate com­ position which represents an optimum material for all types of formations or the quantity utilized in treating the formation. However, effective aqueous silicate solutions of the present invention generally comprise, from about 3 to about 55 percent, preferably about 6 to about 36 percent, by weight of an aqueous alkali metal silicate having an alkali metal oxide to silicon dioxide weight ratio in the range of from about 0.5 to 1 to about 3.5 to 1 and the alkali metal is preferably sodium or potassium; about 1.5 to about 25 percent by weight reducing sugar; and the balance of the aqueous silicate solution being added water (water in addition to that separately admixed with alkali metal silicate, reducing sugar and, optionally, reactive salt). No water need be added or it may be present in an amount of 0.5 to about 16 times the volume of the aqueous commercial silicate used. Upon the disassociation of the gelation acti­ vators, acid groups or acid equivalent groups are produced which react with the aqueous silicate solution to lower the pH thereof and cause the gelation or polymerization thereof. That is, when the pH of the aqueous silicate solution is lowered by the activator to a value within the range of from about 7 to about 12.2, the gelation phenomenon takes place. This, in effect, reduces the pH of the concentrated aqueous silicate solution below the range of from about 10 to about 13, which is required for a stable aqueous silicate mixture. The aqueous silicate solutions are activated at temperatures in the range of from about 120°F to about 170°F (49 to 77°C). At temperatures below 120°F (49°C), the activators produce aqueous silicate-activa­ tor mixtures with good shelf life and low risk of premature gelation. The temperature of the thermally activated aqueous silicate compositions of the present inven­ tion can be raised to a level causing the gelation of the compositions using a variety of methods. In a grouting process, the aqueous silicate composition can be mixed with the activator, applied to a substrate which is to be grouted, and the mixtures can be heated to cause the activator to react and gel the silicate composition. The heating of the silicate composition can be accomplished using radiant light heat or heat created by other tech­ niques such an electromagnetic field. In carrying out subterranean well formation treatments in accordance with this invention, pre­ ferably, an aqueous silicate solution and an aqueous solution containing the reducing sugars are mixed together. The reducing sugar brings about gelation of the solution at the temperature level to which the mixture is heated in the formation, i.e., a temperature from about 120°F to about 170°F (49 to about 77°C). Upon being introduced into the formation, the formation heat causes the temperature of the silicate composition to rise to the level necessary for the activator to react and gel the silicate. If the formation temperature is well above the activator reaction temperature, it may be desirable to cool formation prior to the application or injection of the silicate mixtures to delay gela­ tion or insure against premature gelation. With highly concentrated silicate mixtures, contamination by salts, acid, etc., must be care­ fully avoided and the mixtures should be carefully and uniformly mixed with the activator and any optional materials, such as reactive salts. For most applications, the activator is preferably added to and mixed with the silicate solution as dry material. The concentrated aqueous silicate is also typically diluted to reduce the viscosity for easier application and pumping. As will be understood by those skilled in the art, the particular advantages of the present invention resides in the ability to provide a pre­ dictable delay in the gelling reaction of the aqueous silicate composition-containing the gela­ tion activator. In addition, the gelation activa­ tor is a one component system consisting essentially of a reducing sugar and thus does not require the addition of additional components, such as oxidizers and the like. The following examples will serve to more comprehensively illustrate the principles of the invention, but are not intended to limit the bounds of the invention. EXAMPLE I Samples of aqueous silicate compositions con­ taining the gelation initiator were prepared. The solutions had a total volume of 100 ml and con­ tained 16 percent by volume of a concentrated aqueous sodium silicate, which is described as Grade 40 in the SODIUM SILICATE HANDBOOK and con­ tains about 38 parts solids per 100 parts con­ centrate with a ratio of 3.22 moles of SiO₂ per mole of Na₂O and a pH of about 13, various amounts of lactose, and sufficient water to produce a total volume of 100 ml. Samples of the silicate solutions were placed in a constantly stirred heat bath and maintained at various temperatures. The gel time of the aqueous silicate solutions was then measured. The results of these tests are shown in Table I. EXAMPLE II A series of tests were carried out by pre­ paring a 50 ml aqueous silicate solution comprising 16 ml of concentrated aqueous silicate, (Grade 40), 7.2 grams of lactose, and tap water. A second 50 ml solution was prepared which contained various amounts of CaCl₂. The second solution was added to the first solution with rapid stirring. The com­ bined mixtures were placed in a constantly heated water bath at various temperatures. The gel time was then measured. The results of these tests are shown in Table II. The invention is not limited to the above-­ described specific embodiments thereof; it must be understood therefore, that the detail involved in the descriptions of these embodiments is presented for the purposes of illustration only, and that reasonable variations and modifications, which will be apparent to those skilled in the art, can be made of this invention without departing from the spirit and scope thereof.

Claims: 1. A method of forming a solidified silicate from an aqueous silicate solution, which method comprises mixing an aqueous solution containing an alkali metal silicate with a thermally responsive gelation activator selected from lactose, dextrose, fructose, galactose, mannose, maltose, xylose and mixtures of two or more thereof; and activating said gelation activator by effecting a thermal change in said aqueous silicate solution whereby a solidi­ fied silicate is formed. 2. A method according to claim 1, wherein said alkali metal silicate has a molar ratio of silicon dioxide to alkali metal oxide of from about 0.5 to 1 to about 3.5 to 1. 3. A method according to claim 1 or 2, wherein said alkali metal is sodium or potassium, or a mixture of sodium and potassium is present. 4. A method according to claim 1, 2 or 3, wherein said thermally responsive gelation activator is present in said composition in an amount of from about 10 to about 300 percent by weight of the alkali metal silicate. 5. A method according to any of claims 1 to 4, wherein said composition further comprises a reactive salt capable of reaction with the alkali metal silicate. 6. A method according to any of claims 1 to 5, wherein in said alkali metal silicate, the mole ratio of SiO₂ to Na₂O is about 3.22:1. 7. A method according to any of claims 1 to 6, wherein said alkali metal silicate is present in said composition is an amount of from about 3 to about 55 percent by weight of the composition. 8. A method according to any of claims 1 to 7, wherein said aqueous solution containing said alkali metal silicate is introduced into a subterranean formation before activation of said gelation activator to form a solidified gel in said subterranean formation.

Inventors: SMITH, WILLIAM H., VINSON, EDWARD F.
Applicants: HALLIBURTON COMPANY
Application year: 1986
Main classification: E21B33
IPC codes: C09K8