Well cement compositions and their use

Abstract: Cement compositions for cementing a subterranean zone penetrated by a well bore, comprise Portland cement, 30% to 60% water, 1% to 30% aqueous colloidal silicic acid with particles 300 to 700 m²/g, and 0.1% to 10% of a fluid loss additive which is a graft lignin or lignite polymer, an aqueous solution of the reaction product of polyethyleneimine and a sulfonated organic compound or a copolymer of AMPS and N,N-dimethylacrylamide, the percentages being by weight of the dry cement.

Description: The present invention relates to a well cement composition, and to a method of using the compositions in cementing oil and gas wells. In cementing operations carried out in oil, gas and other wells, a hydraulic cement and various additives are mixed with sufficient water to form a pumpable slurry, and the slurry is pumped into a subterranean zone to be cemented by way of the well bore penetrating the zone. After placement, the cement slurry sets into a hard mass. In primary cementing whereby casing and/or one or more liners are bonded within the well bore, the cementing is accomplished by introducing a cement composition into the annular space between the casing and/or liners and the well bore. Generally, the cement composition is pumped downwardly within the casing and/or liners to the bottom thereof and then upwardly into the annulus. In wells which are drilled into or through high pressure formations, it is necessary that the cement compositions used in carrying out cementing operations in the formations have high densities in order to provide high hydrostatic pressure and to thereby prevent blow-outs. In wells which are drilled into or through low pressure formations, it is generally inadvisable to expose the formations to high hydrostatic pressures in that the formations may break down and the cement compositions lost. Thus, in cementing wells drilled into and through low pressure formations, lightweight cement compositions are advantageously utilized. In most wells, one or more of the subterranean formations penetrated by the well bore contain gas under pressure. When primary cementing operations are carried out in the annulus, the gas may penetrate the cement composition whereby gas migration occurs. Gas migration generally starts during the setting process of the cement composition, i.e., during the time the cement composition changes from a hydrostatic fluid to a solid state body. If the cement composition is not able to resist the gas pressure during the setting process, channels can be formed in the partially cured composition whereby gas flows through the column between formations and/or to the surface. In order to produce both heavyweight and lightweight cement compositions having improved properties whereby the compositions resist gas migration, have low strength retrogression at high temperatures and do not readily settle or segregate, finely divided amorphous silica dust has heretofore been included in the cement compositions. For example, United States Patent No. Re.32,742 issued cn September 6, 1988 discloses a lightweight well cement composition in which amorphous silica dust obtained during the electrothermal preparation of ferrosilicon or the like is included therein. Such silica dust particles typically have specific surface areas of from 18 to 22 square meters per gram (m²/g). Upon and during hardening, the cement composition is substantially gas tight (prevents gas migration) and provides high compressive strength. WO 90/11977 describes a procedure for the admixture of silicon oxide to a hydraulic cement slurry, particularly for well cementing, and is characterized by amorphous silica with particles smaller than 1 micrometer being mixed with water to a liquid micro-silica, a silica flour with particles from 2 to 200 micrometers being mixed in said liquid micro-silica and the thereby obtained silica mixture being added to cement slurry directly in a mixing tank. United States Patent No. 4,935,060 issued June 19, 1990 discloses a high density hydraulic cement composition which is gas tight, has a very low strength retrogression at high temperature and has substantially no tendency to settle or segregate. The cement composition contains amorphous silica dust particles which have a specific surface area in the range of from about 15 m²/g to about 30 m²/g. While the foregoing and other prior art cement compositions have achieved varying degrees of success, there is a need for improved cement compositions having both low and high densities which have reduced settling tendencies, better strengths, enhanced fluid loss properties and which prevent gas migration. We have now devised certain improved cement compositions. According to the present invention, there is provided a well cement composition comprising: (a) Portland hydraulic cement; (b) water in an amount of from 30% to 60% by weight of dry cement; (c) an aqueous colloidal silicic acid suspension wherein the colloidal silicic acid particles in the suspension have a specific surface area of from 300 m²/g to 700 m²/g, the colloidal silicic acid suspension being present in the composition in an amount of from 1% to 30% by weight of dry cement; and (d) a fluid loss control additive selected from a graft lignin or lignite polymer, an aqueous solution of the reaction product of polyethyleneimine and one or more sulfonated organic compounds and a copolymer of AMPS R and N,N-dimethylacrylamide, the additive bring present in the composition in an amount of from 0.1% to 10% by weight of the dry cement. The invention also provides a method of cementing in a subterranean zone penetrated by a well bore, which method comprises the steps of forming a pumpable cement composition comprising water, Portland hydraulic cement and an aqueous colloidal silicic acid suspension wherein the colloidal silicic acid particles in the suspension have a specific surface area in the range of from 300 m²/g to 700 m²/g, the colloidal silicic acid suspension being present in the composition in an amount of from 1% to 30% by weight of the dry cement; and pumping the cement composition into the zone by way of the well bore. The improved well cement compositions of the present invention are pumpable aqueous hydraulic cement slurries comprised of components which make the compositions substantially gas tight, i.e., impervious to gas migration, highly stable, i.e., very little or no settling of solids or separation of free water takes place, have very low fluid loss and have excellent gel and compressive strengths. The cement compositions are basically comprised of hydraulic cement, sufficient water to form a pumpable slurry and an aqueous colloidal silicic acid suspension. While various hydraulic cements can be utilized in forming the compositions, Portland cement is preferred and can be, for example, one or more of the various Portland cements identified as API Classes A through H and J cements. These cements are defined in the "API Specification for Materials and Testing for Well Cements", API Specification 10 of the American Petroleum Institute. The water used can be fresh water, saturated or unsaturated salt water or seawater, and is generally present in the cement compositions in an amount of from 30% to 60% by weight of the dry cement utilized. However, as will be understood, under particular circumstances the particular quantity of water used can vary from the aforesaid amounts. The aqueous colloidal silicic acid suspension included in the cement compositions in accordance with this invention preferably contains silicic acid particles, expressed as silica, in an amount in the range of from 2% to 60% silica by weight of solution, more preferably from 4% to 30% silica by weight. The silicic acid particles in the suspension are generally of a size under about 20 nanometers (nm), more preferably a size ranging from 10 nm down to 1 nm. The specific surface area of the particles is in the range of from 300 m²/g to 700 m²/g. The silicic acid suspension is preferably stabilized with an alkali whereby it has a molar ratio of SiO₂ to M₂O (wherein M is an ion selected from Na, K, Li and NH₄) of from 10:1 to 300:1, more preferably of from 15:1 to 100:1. Generally, the aqueous silicic acid suspension employed includes silicic acid particles which have a maximum active surface area and a well defined small size averaging from 4 nm to 9 nm. A particularly preferred aqueous colloidal silicic acid suspension is one wherein the silicic acid particles have an average specific surface area of about 500 m²/g, the particles have an average size of about 5.5 nm and the suspension contains silicic acid particles, expressed as silica, in an amount of about 15% silica by weight of the suspension. The aqueous silicic acid suspension is generally included in a cement composition of this invention in an amount in the range of from 1.0% to 30% by weight of dry cement in the composition. When the aqueous silicic acid suspension is utilized in lightweight cement compositions, greater amounts of the suspension are generally used as compared to when the aqueous silicic acid suspension is included in other cement compositions to make them gas tight, improve their stabilities, etc. Because of the very high specific surface area and small size of the colloidal silicic acid particles, a much smaller quantity of such particles are required in cement compositions to produce the desired results as compared to heretofore used fine silica cement composition additives. In addition, because the colloidal silicic acid particles are suspended in an aqueous medium, the particles are readily added to and dispersed in a cement composition using a minimum of mixing. When the most preferred aqueous silicic acid suspension described above wherein the suspension contains silicic acid particles having an average specific surface area of about 500 m²/g in an amount equivalent to about 15% silica by weight of the suspension is used, it is included in a cement composition in an amount in the range of from 2% to 15% by weight of cement in the composition, more preferably in an amount of about 10% by weight of cement in the composition. The cement compositions of the present invention also preferably include fluid loss control additives which reduce fluid losses from the cement compositions into surrounding subterranean formations or zones. While a variety of fluid loss control additives well known to those skilled in the art can be utilized, a particularly suitable such additive is comprised of a graft lignin or lignite polymer of the type disclosed in United States Patent No. 4,676,317 issued January 30, 1987. Generally, such a graft polymer is comprised of a backbone of at least one member selected from the group consisting of lignin, lignite and their salts, and a grafted pendant group comprising at least one member selected from the group consisting of 2-acrylamido-2-methylpropanesulfonic acid (AMPS®), acrylonitrile, N,N-dimethylacrylamide, acrylic acid and N,N-dialkylaminoethylmethacrylate wherein the alkyl radical is selected from methyl, ethyl and propyl radicals. Another preferred fluid loss additive is an aqueous solution of the reaction product of polyethyleneimine and one or more sulfonated organic compounds described in United States Patent No. 4,742,094 issued May 3, 1988. Generally, the fluid loss additive is comprised of an aqueous solution of the reaction product formed by admixing polyethyleneimine having a molecular weight above about 50,000 and sulfonated organic compounds comprising an admixture of lignosulfonic acid salts having Na, Ca or NH₄ as the associated cation, together with naphthalene sulfonic acid condensed with formaldehyde having a molecular weight above about 5000. The ratio by weight of the polyethyleneimine to the sulfonated compounds is in the range of from 1:1.4 to 7.5:1, and the ratio by weight of the lignosulfonic acid salt to the naphthalene sulfonic acid condensed with formaldehyde is in the range of from 1:5 to 5:1. Yet another preferred fluid loss additive is the copolymer or copolymer salt of 2-acrylamido, 2-methylpropanesulfonic acid (AMPS®) and N,N-dimethylacrylamide (NNDMA) described in U.S. Patent No. 4,555,269 issued November 26, 1985. Generally, the copolymer or copolymer salt has a ratio of AMPS® to NNDMA of between 1:4 to 4:1. The above described graft lignin or lignite polymer is generally added to a cement composition of the present invention in an amount of 0.25% to 5% by weight of the dry cement in the composition. When the aqueous solution of the reaction product of polyethyleneimine and one or more sulfonated organic compounds is utilized, it is generally added to the cement composition in an amount in the range of from 2.5% to 10% by weight of dry cement in the composition. When the AMPS® - NNDMA copolymer or copolymer salt is used, it is added to the cement composition in an amount of 0.1% to 1.5% by weight of cement. In some applications, e.g., when the cement composition is utilized in a hot deep well, it is necessary or desirable that a set retarding additive be included in the cement composition. The addition of a set retarder to a cement composition increases the time from when the composition is prepared to when it sets thereby allowing it to be pumped for a longer period of time, etc. A variety of set retarding additives well known to those skilled in the art can be utilized in the cement compositions of this invention. A preferred set retarding additive which allows rapid development of cement compressive strength after placement is comprised of a copolymer of 2-acrylamido, 2-methylpropanesulfonic acid (AMPS®) and acrylic acid. The copolymer generally comprises from 40 to 60 mole percent AMPS® with the balance comprising acrylic acid. It preferably has an average molecular weight below about 5000 such that a 10% aqueous solution of the copolymer has a Brookfield viscosity reading at 20 rpm of the U.L. adapter spindle in the range of from 2 to less than 5 centipoise. Preferably, the copolymer comprises from 45 to 55 mole percent AMPS®, and most preferably about 50 mole percent AMPS®. Other set retarding additives which can be used are lignosulfonates, borates or organic acids such as gluconic acid, citric acid and the like. Of these, a set retarder comprised of lignosulfonate is preferred. When a set retarding copolymer of AMPS® and acrylic acid is utilized, it is preferably included in a cement composition of this invention in an amount in the range of from 0.1% to 5.0% by weight of dry cement utilized. When a lignosulfonate set retarding additive is used, it is also preferably included in the cement composition in an amount of 0.1% to 5.0% by weight of dry cement utilized. In both cases, in order to enhance the set retarding ability of the set retarding additives, a set retarder intensifier such as tartaric acid or a salt thereof can be included in the cement composition in an amount in the range of from 0.2% to 5.0% by weight of dry cement used. When a lignosulfonate set retarding additive is included in the cement compositions of the present invention, a tartaric acid intensifier is also preferably included. A well cement composition of the present invention having improved properties is comprised of water, hydraulic cement and an aqueous colloidal silicic acid suspension wherein the colloidal silicic acid particles in the suspension have specific surface areas in the range of from 300 m²/g to 700 m²/g, and most preferably about 500 m²/g. The aqueous colloidal silicic acid suspension preferably contains silicic acid particles, expressed as silica, in an amount in the range of from 4% to 30% SiO₂ by weight of the suspension, most preferably 15% by weight. When a fluid loss control additive is included in the cement composition to reduce fluid loss, the additive is preferably selected from the group consisting of a graft lignin or lignite polymer, an aqueous solution of the reaction product of polyethyleneimine and one or more sulfonated organic compounds and a copolymer or copolymer salt of 2-acrylamido, 2-methylpropanesulfonic acid and N,N-dimethylacrylamide. The fluid loss control additive is added to the cement composition in an amount in the range of from 0.1% to 10% by weight of the dry cement therein. When a set retarding additive is included in the cement composition, it is preferably selected from the group consisting of lignosulfonate plus tartaric acid and a copolymer of 2-acrylamido, 2-methylpropanesulfonic acid and acrylic acid. The set retarding additive is included in the cement composition in an amount in the range of from 0.1% to 10% by weight of dry cement utilized. In accordance with the improved methods of the present invention for cementing in a subterranean zone penetrated by a well bore, an improved pumpable cement composition of this invention is first formed, followed by pumping the cement composition into the subterranean zone by way of the well bore. As indicated above, when placed in subterranean zones, the improved cement compositions of this invention are gas tight, i.e., prevent gas migration prior to and after setting, and have outstanding stability. When the compositions are utilized at low temperatures and have relatively high water - cement ratios, the presence of the aqueous colloidal silicic acid suspension accelerates the setting of the cement compositions. In order to further illustrate the improved cement compositions and methods of the present invention, the following examples are given. Example 1 A number of test cement slurries were prepared utilizing API Class G Portland cement. The slurries were prepared by dry blending the dry components with the cement prior to the addition of water. Fresh water (except where noted differently) was then mixed with the dry blends to form slurries in a Waring blender. The test slurries produced are described in Table I below. The rheologies and gel strengths of the slurries were determined using a Fann Model 35 ® viscometer in accordance with the "API Specification for Materials and Testing for Well Cements", API Specification 10 , of the American Petroleum Institute. In addition, thickening time, fluid loss and free water tests were run in accordance with the above mentioned API Specification at a bottom hole circulating temperature (BHCT) of 25°C (77°F). The rheology and gel strength test results are given in Table II below and the thickening time, fluid loss and free water tests are given in Table III below. Test Cement Slurry No. Dispersant , % Fluid Loss Control Additive , % Aqueous Colloidal Silicic Acid Suspension , dm³/kg Water Ratio, dm³/kg (gal/sk) Slurry Specific Gravity 1 --- --- 0.044(0.51) 1.018(11.70) 1.5 2 --- --- 0.059(0.68) 1.014(11.66) 1.5 3 --- --- 0.059(0.68) 1.087(12.49) 1.5 4 --- --- 0.059(0.68) 1.049(12.06) 1.5 5 0.5 0.5 0.069(0.79) 0.852(9.79) 1.56 6 0.5 0.5 0.069(0.79) 0.850(9.77) 1.56 7 0.7 0.7 0.088(1.01) 0.840(9.65) 1.56 8 0.7 0.7 0.098(1.13) 0.813(9.34) 1.56 9 0.7 0.7 0.098(1.13) 0.832(9.56) 1.56 Test Cement Slurry No. Temp., °C(°F) Fann Readings at rpm Gel Strength 300 200 180 100 90 60 30 6 3 10 sec 10 min 1 25(77) 16.5 14 13 11 10.5 9 8 8 7 - - 2 25(77) 22 19 18.5 16 15 14 12.5 11 10 10.5 14.5 3 25(77) 25 22 21 18 17 16 15 13 11 15 24 4 25(77) 20 17 17 14 14 13 12 11 9 7 12 5 25(77) 52 50 48 49 48 49 51 57 55 33 41 6 25(77) 32 23 21 14 13 9.5 6 2 1 2 3 7 25(77) 47 34.5 32 21 19 14 9 3 2 2.5 5 8 25(77) 47 35 32 21 20 15 9 5 3 3 5 9 25(77) 70 66 - 69 - - - 93 91 60 - Test Cement Slurry No. Thickening Time, hrs: mins Fluid Loss, ml/30 min Free Water, % 1 5:00 --- 3.2 2 --- --- 1.9 3 5:00 + --- 0.9 4 --- --- 1.0 5 --- --- --- 6 --- --- --- 7 5:48 34 0 8 4:26 --- --- 9 --- --- --- Example 2 Additional test slurries of the present invention were prepared in accordance with the procedure given in Example 1 above, the components and quantities of which are set forth in Table IV. Rheology and gel strength tests performed using the slurries are given in Table V below and thickening time, fluid loss and free water tests at a BHCT of 25°C (77°F) are set forth in Table VI. Test Cement Slurry No. Dispersant , % Fluid Loss Control Additive , dm³/kg (gal/sk) Aqueous Colloidal Silicic Acid Suspension , dm³,kg (gal/sk) Set Retarder , dm³/kg (gal/sk) Set Retarder , dm³/kg (gal/sk) Water Ratio, dm³/kg (gal/sk) Slurry Specific Gravity 10 0.5 0.049 0.56 0.039 0.45 --- --- --- --- 0.347 3.99 1.92 11 0.5 0.049 0.56 0.039 0.45 --- --- 0.006 0.07 0.341 3.92 1.92 12 0.5 0.049 0.56 0.039 0.45 0.007 0.08 --- --- 0.341 3.92 1.92 13 0.75 0.049 0.56 0.039 0.45 0.007 0.08 --- --- 0.389 4.47 1.92 14 1.0 0.049 0.56 0.039 0.45 0.007 0.08 --- --- 0.338 3.89 1.92 Test Cement Slurry No. Temp., °C(°F) Fann Readings at rpm Gel Strength 300 200 180 100 90 60 30 6 3 10 sec 10 min 10 25(77) - - - - - - - - - - - 11 25(77) 100 76 71 48 45 36 25 16 15 33 111 12 25(77) 141 111 106 76 73 61 47 39 35 41 65 13 25(77) 107 81 76 53 50 40 30 21 19 29 45 14 25(77) 84 63 59 40 38 31 22 14 13.5 20 31 Test Cement Slurry No. Thickening Time, hrs: mins Fluid Loss, ml/30 min Free Water, % 10 1:26 --- --- 11 --- 88 0 12 2:59 100 0 13 --- 98 --- 14 3:43 117 0 Example 3 Additional test slurries were prepared in accordance with the procedure set forth in Example 1, the components and quantities of which are given in Table VII below. Test Cement Slurry No. Dispersant , % Fluid Loss Control Additive , % Aqueous Colloidal Silicic Acid Suspension , dm³/kg (gal/sk) Set Retarder , dm³/kg (gal/sk) Water Ratio, dm³/kg (gal/sk) Slurry Specific Gravity 15 --- 0.7 0.087 1.0 0.012 0.14 0.974 11.2 1.5 16 --- 0.7 0.087 1.0 0.012 0.14 1.016 11.68 1.5 17 0.6 0.5 0.026 0.3 0.035 0.04 0.421 4.84 1.9 18 0.6 0.5 0.026 0.3 0.035 0.04 0.386 4.44 1.9 The rheologies at 32°C (90°F) and the results of thickening time, fluid loss and free water tests at a BHCT of 32°C (90°F) are given in Tables VIII and IX below, respectively. Test Cement Slurry No. Temp., °C(°F) Fann Readings at rpm 300 200 180 100 90 60 30 6 3 15 32(90) 23 17 16 10 9.5 7 4.5 4 2 16 32(90) 29 22 21 14 13 10 7 3 2 17 32(90) 98 70 64 40 37 27 16 8 4 18 32(90) 89 63 58 36 33 24 14 9 4 Test Cement Slurry No. Thickening Time, hrs: mins Fluid Loss, ml/30 min Free Water, % 15 7:45 46 0 16 8:00 + 66 0 17 5:04 98 0 18 4:20 100 0 Example 4 Additional test slurries were prepared in accordance with the procedure set forth in Example 1, the components and quantities of which are set forth in Table X below. Test Cement Slurry No. Dispersant , % Fluid Loss Control Additive , % Aqueous Colloidal Silicic Acid Suspension , dm³/kg (gal/sac) Set Retarder , dm³/kg (gal/sac) Water Ratio, dm³/kg (gal/sac) Slurry Specific Gravity 19 --- 0.007 0.08 0.088 1.01 --- --- 0.816 9.38 1.56 20 --- 0.049 0.56 0.039 0.45 0.012 0.14 0.337 3.87 1.92 21 0.25 0.049 0.56 0.039 0.45 0.012 0.14 0.336 3.86 1.92 22 0.50 0.049 0.56 0.039 0.45 0.007 0.08 0.339 3.90 1.92 23 0.50 0.049 0.56 0.039 0.45 0.010 0.11 0.337 3.87 1.92 24 0.50 0.049 0.56 0.039 0.45 0.012 0.14 0.334 3.84 1.92 25 0.75 0.049 0.56 0.039 0.45 0.012 0.14 0.333 3.83 1.92 Rheology and gel strength tests at temperatures of 25°C (77°F) and 71°C (160°F) were conducted on the slurries except for slurry No. 19 which was tested at 66°C (150°F) only, and thickening time, fluid loss and free water tests were conducted at a BHCT of 66°C (150°F) for slurry No. 19 and at 71°C (160°F) for slurries 20-25. The results of these tests are given in Tables XI and XII below. Test Cement Slurry No. Temp., °C(°F) Fann Readings at rpm Gel Strength 300 200 180 100 90 60 30 6 3 10 sec 10 min 19 66(150) 32 24 22 15 14 10 7 2 1 2 3 20 25(77) 104 99 - 66 - - - 50 55 92 300 + 20 71(160) 97 73 67 47 43 35 25 15 16 14 104 21 25(77) 81 63 70 41 45 38 31 11 20 80 300 + 21 71(160) 80 60 57 38 36 29 20 9 8 9 74 22 25(77) 70 52 53 31 32 25 17 5 5 9 162 22 71(160) 45 32 30 19.5 18.5 13 8 3 2 3 15 23 25(77) - - - - - - - - - - - 23 71(160) - - - - - - - - - - - 24 25(77) 77 60 65 39 42 35 26 10 10 55 300 + 24 71(160) 80 62 61 41 39 31 22 12 12 10 79 25 25(77) 53 39 39 22 22 16 10 3 2 4.5 158 25 71(160) 63 47 45 29 28 22 15 6 5 6 79 Test Cement Slurry No. Thickening Time, hrs: mins Fluid Loss, ml/30 min Free Water, % 19 --- 70 0 20 --- --- --- 21 --- --- --- 22 4:40 58 0 23 8:32 --- --- 24 --- --- --- 25 --- 6 0 Example 5 Additional test slurries of the present invention were prepared in accordance with the procedure described in Example 1, the components and quantities of which are given in Table XIII below. Test Cement Slurry No. Fluid Loss Additive , dm³/kg (gal/sac) Fluid Loss Additive , dm³/kg (gal/sac) Aqueous Colloidal Silicic Acid Suspension , dm³/kg (gal/sac) Set Retarder , dm³/kg (gal/sac) Water Ratio, dm³/kg (gal/sac) Slurry Specific Gravity 26 --- --- 0.049 (0.56) 0.039 (0.45) 0.018 (0.21) 0.333 (3.83) 1.92 27 0.049 (0.56) --- --- 0.039 (0.45) 0.012 (0.14) 0.334 (3.84) 1.92 Rheology and static gel strength tests at 91°C (195°F), and thickening time, fluid loss and free water tests at a BHCT of 91°C (195°F) were run on the slurries, the results of which are given in Tables XIV and XV below, respectively. Test Cement Slurry No. Temp., °C(°F) Fann Readings at rpm Gel Strength 300 200 180 100 90 60 30 6 3 10 sec 10 min 26 91(195) 34 25 24 15 14 11 6.5 2.5 1.5 3 36 27 91(195) 39 29 27 17 16 - 7.5 3 2 3 7 Test Cement Slurry No. Thickening Time, hrs: mins Fluid Loss, ml/30 min Free Water, % 26 4:55 32 0 27 4:06 78 0 Compressive strength tests were conducted in accordance with the above mentioned API Specification using a number of the test cement slurries described in the preceding examples at various temperatures. The results of these tests are set forth in Table XVI below. Test Cement Slurry No. TEMP °C (°F) COMPRESSIVE STRENGTH MPa(psi) 8 hr 12 hr 16 hr 18 hr 24 hr 36 hr 96 hr 2 28 (82) ---- -- 0.34 (50) ---- --- 0.76 (110) 0.80 (116) 1.62 (235) 3.10 (450) 3 28 (82) 0.55 (80) 0.83 (120) 1.03 (150) 1.24 (180) 1.45 (210) ---- --- ---- --- 7 25 (77) ---- -- ---- --- 1.03 (150) 1.48 (215) 1.83 (265) 2.76 (400) ---- --- 8 25 (77) 0.28 (40) 0.79 (115) 1.10 (160) 1.31 (190) 1.79 (260) ---- --- ---- --- 14 25 (77) 0.69 (100) 3.27 (475) 5.51 (800) 1.31 (950) 8.61 (1250) 11.71 (1700) ---- --- 15 38 (100) ---- --- ---- --- ---- --- ---- --- 3.45 (500) ---- --- ---- --- 16 38 (100) 0.34 (50) 0.90 (130) 1.38 (200) 1.58 (230) 2.07 (300) ---- --- ---- --- 17 38 (100) 0.69 (100) 5.51 (800) 8.61 (250) 9.65 (1400) 12.23 (1775) ---- --- ---- --- 18 38 (100) ---- --- ---- --- 11.37 (1650) ---- --- ---- --- ---- --- ---- --- 19 66 (150) 1.72 (250) 2.48 (360) 3.03 (440) 3.45 (500) 3.79 (550) 4.48 (650) ---- --- 22 71 (160) ---- --- 11.02 (1600) ---- --- ---- --- ---- --- ---- --- ---- --- 26 91 (195) ---- --- 14.47 (2100) ---- --- 19.29 (2800) 20.67 (3000) ---- --- ---- --- 27 91 (195) ---- --- 12.40 (1800) ---- --- 15.16 (2200) ---- --- ---- --- ---- --- From the test results set forth in the above examples it can be seen that the improved cement compositions of the present invention do not readily settle or form free water and they exhibit good gel and compressive strength development properties.

Claims: A well cement composition comprising: (a) Portland hydraulic cement; (b) water in an amount of from 30% to 60% by weight of dry cement; (c) an aqueous colloidal silicic acid suspension wherein the colloidal silicic acid particles in the suspension have a specific surface area of from 300 m²/g to 700 m²/g, the colloidal silicic acid suspension being present in the composition in an amount of from 1% to 30% by weight of dry cement; and (d) a fluid loss control additive selected from a graft lignin or lignite polymer, an aqueous solution of the reaction product of polyethyleneimine and one or more sulfonated organic compounds and a copolymer of AMPS ® and N,N-dimethylacrylamide, the additive bring present in the composition in an amount of from 0.1% to 10% by weight of the dry cement. A composition according to claim 1, further comprising a set retarder selected from lignosulfonate plus tartaric acid and an AMPS R - acrylic acid copolymer, the retarder being present in the composition in an amount from 0.1% to 10% by weight of the dry cement. A composition according to claim 1 or 2, wherein the colloidal silicic acid suspension contains silicic acid particles, expressed as silica, in an amount of from 4% to 30% silica by weight of the suspension, and wherein the silicic acid particles have an average size of from 1 nm to 10 nm and said colloidal silicic acid suspension is present in the composition in an amount of from 2% to 15% by weight of the dry cement. A composition according to claim 3, wherein the colloidal silicic acid suspension contains silicic acid particles, expressed as silica, in an amount of 15% silica by weight of said suspension, said silicic acid particles have an average size of 5.5 nm and said colloidal silicic acid suspension is present in said composition in an amount of 10% by weight of dry cement. A composition according to claim 1,2,3 or 4, wherein the colloidal silicic acid particles have an average specific surface area of about 500 m²/g. A method of cementing in a subterranean zone penetrated by a well bore, which method comprises the steps of forming a pumpable cement composition comprising water, Portland hydraulic cement and an aqueous colloidal silicic acid suspension wherein the colloidal silicic acid particles in the suspension have a specific surface area in the range of from 300 m²/g to 700 m²/g, the colloidal silicic acid suspension being present in the composition in an amount of from 1% to 30% by weight of the dry cement; and pumping the cement composition into the zone by way of the well bore. A method according to claim 6, wherein the cement composition further comprises a fluid loss control additive selected from a graft lignin or lignite polymer, an aqueous solution of the reaction product of polyethyleneimine and one or more sulfonated organic compounds and a copolymer of AMPS R and N,N-dimethylacrylamide, the additive being present in the composition in an amount of from 0.1 to 10% by weight of the dry cement. A method according to claim 7, wherein the cement composition further includes a set retarder selected from lignosulfonate plus tartaric acid and an AMPS R - acrylic acid copolymer, present in an amount of from 0.1 to 10% by weight of the dry cement in the composition. A method according to claim 6,7 or 8, wherein the cement composition is as claimed in any of claims 1 to 5.

Inventors: BJORDAL AUDUN, OLAUSSEN STEIN, SOLLAND GEIR, BJORDAL, AUDUN, OLAUSSEN, STEIN, SOLLAND, GEIR
Applicants: HALLIBURTON CO, HALLIBURTON COMPANY
Application year: 1992
Main classification: E21B33
IPC codes: C04B14, C09K8, C04B28