Cement compositions and methods utilizing nano-hydraulic cement

Abstract
An exemplary method includes introducing a treatment fluid comprising nano-hydraulic cement into a subterranean formation. The treatment fluid may include a drilling fluid, a completion fluid, a stimulation fluid, a well clean-up fluid or a cement composition. Another example method comprises introducing a cement composition comprising nano-hydraulic cement, hydraulic cement, and water into a subterranean formation; and allowing the cementing composition to set in the subterranean formation. An example well treatment fluid comprises nano-hydraulic cement.
Description
BACKGROUND

The present invention relates to well treatment fluids and methods utilizing nano-particles and, in certain embodiments, to well cement compositions and methods utilizing nano-hydraulic cement.


In general, well treatments include a wide variety of methods that may be performed in oil, gas, geothermal and/or water wells, such as drilling, completion and workover methods. The drilling, completion and workover methods may include, but are not limited to, drilling, fracturing, acidizing, logging, cementing, gravel packing, perforating and conformance methods. Many of these well treatments are designed to enhance and/or facilitate the recovery of desirable fluids from a subterranean well. Examples of such well treatments are discussed hereinbelow.


In cementing methods, such as well construction and remedial cementing, well cement compositions are commonly utilized. For example, in subterranean well construction, a pipe string (e.g., casing and liners) may be run into a well bore and cemented in place using a cement composition. The process of cementing the pipe string in place is commonly referred to as “primary cementing.” In a typical primary cementing method, a cement composition may be pumped into an annulus between the walls of the well bore and the exterior surface of the pipe string disposed therein. The cement composition sets in the annular space, thereby forming an annular sheath of hardened, substantially impermeable cement that supports and positions the pipe string in the well bore and bonds the exterior surface of the pipe string to the subterranean formation. Among other things, the annular sheath of set cement surrounding the pipe string functions to prevent the migration of fluids in the annulus, as well as protecting the pipe string from corrosion. Cement compositions also may be used in remedial cementing methods, such as squeeze cementing, repairing casing strings and the placement of cement plugs. In some instances, cement compositions may be used to change the direction of the well bore, for example, by drilling a pilot hole in a hardened mass of cement, commonly referred to as a “kickoff plug,” placed in the well bore.


Hydraulic fracturing is a process commonly used to increase the flow of desirable fluids, such as oil and gas, from a portion of a subterranean formation. Hydraulic fracturing operations generally involve introducing a fracturing fluid into a subterranean formation at or above a pressure sufficient to create or enhance one or more fractures in the formation. Enhancing a fracture includes enlarging a pre-existing fracture in the formation. The fracturing fluid may comprise particulates, often referred to as “proppant” that are deposited in the fractures. The proppant functions to prevent the fractures from fully closing upon the release of pressure, forming conductive channels through which fluids may flow to (or from) the well bore.


Another process that involves the use of particulates is gravel packing. A “gravel pack” is a term commonly used to refer to a volume of particulate materials (such as sand) placed into a well bore to at least partially reduce the migration of unconsolidated formation particulates into the well bore. Gravel packing operations commonly involve placing a gravel pack screen in the well bore neighboring a desired portion of the subterranean formation, and packing the surrounding annulus between the screen and the subterranean formation with particulate materials that are sized to prevent and inhibit the passage of formation solids through the gravel pack with produced fluids. In some instances, a screenless gravel packing operation may be performed.


SUMMARY

The present invention relates to well treatment fluids and methods utilizing nano-particles and, in certain embodiments, to well cement compositions and methods utilizing nano-hydraulic cement.


An embodiment of the present invention provides a method that comprises introducing a treatment fluid comprising nano-hydraulic cement into a subterranean formation.


Another embodiment of the present invention provides a method of cementing in a subterranean formation that comprises introducing a cement composition comprising nano-hydraulic cement and water into the subterranean formation; and allowing the cementing composition to set in the subterranean formation.


Another embodiment of the present invention provides a method of fracturing in a subterranean formation that comprises fracturing the subterranean formation; and introducing a proppant comprising a nano-particle into one or more fractures in the subterranean formation.


Another embodiment of the present invention provides a method of gravel packing in a subterranean formation that comprises depositing a volume of a particulate comprising a nano-particle into a well bore to at least partially reduce the migration of unconsolidated formation particulates into the well bore.


Another embodiment of the present invention provides a method that comprises introducing hydrated nano-hydraulic cement particulates into a subterranean formation.


Another embodiment of the present invention provides a well treatment fluid that comprises nano-hydraulic cement.


The features and advantages of the present invention will be readily apparent to those skilled in the art. While numerous changes may be made by those skilled in the art, such changes are within the spirit of the invention.







DESCRIPTION OF SPECIFIC EMBODIMENTS

The present invention relates to well treatment fluids and methods utilizing nano-particles and, in certain embodiments, to well cement compositions and methods utilizing nano-hydraulic cement.


An embodiment of the cement compositions of the present invention comprises nano-hydraulic cement, hydraulic cement, and water. Those of ordinary skill in the art will appreciate that the embodiments of the cement compositions generally should have a density suitable for a particular application. By way of example, the cement composition may have a density in the range of from about 4 pounds per gallon (“ppg”) to about 20 ppg. In certain embodiments, the cement compositions may have a density in the range of from about 8 ppg to about 17 ppg. Embodiments of the cement compositions may be foamed or unfoamed or may comprise other means to reduce their densities, such as hollow microspheres, low-density elastic beads, or other density-reducing additives known in the art. Those of ordinary skill in the art, with the benefit of this disclosure, will recognize the appropriate density for a particular application.


Nano-hydraulic cements have a variety of applications for well cementing, including both primary and remedial cementing operations. Generally, “nano-hydraulic cement” may be defined as a cement with cement particles having a mean particle size of less than 1 micron. For example, nano-hydraulic cement may have a mean particle size in the range of from about 20 nanometers (“nm”) to about 310 nm, alternatively about 20 nm to about 150 nm, and alternatively about 20 nm to about 100 nm. A suitable nano-hydraulic cement and technique that may be used to measure particle size, in accordance with embodiments of the present invention, is described by S C Halim, T J Brunner, R N Grass, M Bohner and W J Stark, Preparation of an Ultra Fast Binding Cement from Calcium Silicate-Based Mixed Oxide Nanoparticles, NANOTECHNOLOGY 18 (2007) 395701 (6 pp). Among other advantages of using nano-hydraulic cement is that it should provide a cement composition with a lower density and reduced set time. It is believed that the reduced set time of the nano-hydraulic cement may be from early reactivity. In addition, since nano-hydraulic cement particles are small particles, the nano-hydraulic cement should be capable of invading narrow openings that standard cements are unable to access. Accordingly, nano-hydraulic cements may be particularly suitable for use in squeeze cement applications. For example, nano-hydraulic cements may be used to seal voids in a pipe string, cement sheath, or gravel pack. As used herein, the term “void” refers to any type of space, including fractures, holes, cracks, spaces, channels, and the like. It is believed that the nano-hydraulic cement will be able to penetrate voids that are not repairable with larger-ized cements.


In certain embodiments, the treatment fluid comprises nano-hydraulic cement. Generally, any hydraulic cement suitable for use in cementing operations and sized less than 1 micron may be suitable for use as a nano-hydraulic cement in embodiments in the present invention. Suitable hydraulic cements include those classified as Classes A through H according to American Petroleum Institute, API Specification for Materials and Testing for Well Cements, API Specification 10, Fifth Ed., Jul. 1, 1990. In certain embodiments, API Class A, C, G and H nano-hydraulic cements may be preferred. A variety of nano-hydraulic cements are suitable for use, including those comprised of calcium, aluminum, silicon, oxygen, and/or sulfur, which set and harden by reaction with water. Such nano-hydraulic cements include, but are not limited to, Portland cements, pozzolanic cements, gypsum cements, soil cements, calcium phosphate cements, high-alumina content cements, silica cements, high-alkalinity cements, or mixtures thereof.


The nano-hydraulic cement may be present in embodiments of the cement compositions of the present invention in an amount of from about 0.01% to 100% by weight of cementitious material. As used herein, the term “cementitious material” refers to nano-hydraulic cement, hydraulic cement, and cement kiln dust, which set and harden by reaction with water. In some embodiments, the nano-hydraulic cement may be present in the cement compositions of the present invention in an amount of about 1% to 75% by weight of cementitious material. In some embodiments, the nano-hydraulic cement may be present in the cement compositions of the present invention in an amount of about 1% to about 50% by weight of cementitious material. In some embodiments, the nano-hydraulic cement may be present in the cement compositions of the present invention in an amount of about 1% to about 25% by weight of cementitious material.


Embodiments of the present invention may comprise a “hydraulic cement” that has a mean particle size of greater than 1 micron. Generally, any hydraulic cement suitable for use in cementing operations may be suitable for use in the present invention. Suitable hydraulic cements include those classified as Classes A through H according to American Petroleum Institute, API Specification for Materials and Testing for Well Cements, API Specification 10, Fifth Ed., Jul. 1, 1990. In certain embodiments, API Class A, C, G and H hydraulic cements may be preferred. A variety of hydraulic cements may be suitable for use, including those comprised of calcium, aluminum, silicon, oxygen, and/or sulfur, which set and harden by reaction with water. Such hydraulic cements include, but are not limited to, Portland cements, pozzolanic cements, gypsum cements, soil cements, calcium phosphate cements, high-alumina content cements, silica cements, high-alkalinity cements, or mixtures thereof. In some embodiments, the hydraulic cement may be a micro-fine cement (e.g., a micro-fine Portland cement) having a mean particle size of less than about 30 microns, alternatively less than about 17 microns, and alternatively less than about 11 microns. A suitable micro-fine Portland cement composition is described in U.S. Pat. No. 5,125,455, the disclosure of which is incorporated herein by reference.


Where present, the hydraulic cement generally may be included in the cement compositions in an amount sufficient to provide the desired compressive strength, density, and/or cost. In some embodiments, the hydraulic cement may be present in the cement compositions of the present invention in an amount of about 0% to about 99% by weight of cementitious materials. In some embodiments, the hydraulic cement may be present in the cement compositions of the present invention in an amount of about 0% to about 75% by weight of cementitious materials. In some embodiments, the hydraulic cement may be present in the cement compositions of the present invention in an amount of about 0% to about 50% by weight by weight of cementitious materials. In some embodiments, the hydraulic cement may be present in the cement compositions of the present invention in an amount in the range of from about 0% to about 25% by weight of cementitious materials.


In some embodiments, a pozzolanic cement that may be suitable for use comprises fly ash. As used herein, “fly ash” refers to the residue from the combustion of powdered or ground coal, wherein the fly ash carried by flue gases may be recovered, for example, by electrostatic precipitation. A variety of fly ashes may be suitable, including fly ash classified as Class C and Class F fly ash according to American Petroleum Institute, API Specification for Materials and Testing for Well Cements, API Specification 10, Fifth Ed., Jul. 1, 1990. Class C fly ash comprises both silica and lime so that, when mixed with water, it sets to form a hardened mass. Class F fly ash generally does not contain sufficient lime, so an additional source of calcium ions is required for the Class F fly ash to form a cement composition with water. In some embodiments, lime may be mixed with Class F fly ash in an amount in the range of from about 0.1% to about 25% by weight of the fly ash. In some instances, the lime may be hydrated lime. Suitable examples of fly ash include, but are not limited to, “POZMIX® A” cement additive, commercially available from Halliburton Energy Services, Inc., Duncan, Okla.


Where present, the fly ash generally may be included in the cement compositions in an amount sufficient to provide the desired compressive strength, density, and/or cost. In some embodiments, the fly ash may be present in the cement compositions of the present invention in an amount of about 1% to about 75% by weight of cementitious materials. In some embodiments, the fly ash may be present in the cement compositions of the present invention in an amount of about 5% to about 50% by weight of cementitious materials.


In some embodiments, a slag cement that may be suitable for use may comprise slag. As used herein, “slag” refers to a granulated, blast furnace by-product formed in the production of cast iron and generally comprises oxidized impurities found in iron ore. Slag generally does not contain sufficient basic material, so slag cement further may comprise a base to produce a cement composition that may react with water to set to form a hardened mass. Examples of suitable sources of bases include, but are not limited to, sodium hydroxide, sodium bicarbonate, sodium carbonate, lime, and combinations thereof. In certain embodiments, the slag cement may comprise micro-fine slag wherein less than 3 weight % of the slag particles have a particle size of greater than about 7.8 microns. A suitable micro-fine slag composition is described in U.S. Pat. No. 5,026,215, the disclosure of which is incorporated herein by reference.


Where present, the slag cement generally may be included in the cement compositions in an amount sufficient to provide the desired compressive strength, density, and/or cost. In some embodiments, the slag cement may be present in the cement compositions of the present invention in an amount of about 1% to about 99% by weight of cementitious materials. In some embodiments, the slag cement may be present in the cement compositions of the present invention in an amount of about 1% to about 50% by weight of cementitious materials.


The water used in certain embodiments of the cement compositions of the present invention may be freshwater or saltwater (e.g., water containing one or more salts dissolved therein, seawater, brines, saturated saltwater, etc.). In general, the water may be present in an amount sufficient to form a pumpable slurry. In certain embodiments, the water may be present in the cement compositions in an amount in the range of about 33% to about 200% by weight of cementitious materials. In certain embodiments, the water may be present in an amount in the range of about 35% to about 70% by weight of cementitious materials.


In certain embodiments, the cement mixture will comprise cement kiln dust (“CKD”). As used herein, “CKD” refers to a partially calcined kiln feed which may be removed from the gas stream and collected in a dust collector during the manufacturer of cement. The CKD should be included in the cement compositions in an amount sufficient to provide the desired compressive strength, density, and/or cost reduction. In some embodiments, the CKD may be present in the cement compositions of the present invention in an amount of about 0.01% to about 99% by weight of cementitious materials. In some embodiments, the CKD may be present in the cement compositions of the present invention in an amount of about 1% to about 75% by weight of cementitious materials. In some embodiments, the CKD may be present in the cement compositions of the present invention in an amount of about 1% to about 50% by weight of cementitious materials. In some embodiments, the CKD may be present in the cement compositions of the present invention in an amount of about 1% to about 25% by weight of cementitious materials.


In certain embodiments, the cement compositions of the present invention may further comprise metakaolin. Generally, metakaolin is a white pozzolan that may be prepared by heating kaolin clay, for example, to temperatures in the range of from about 600° to about 800° C. In some embodiments, the metakaolin may be present in the cement compositions of the present invention in an amount of about 1% to about 50% by weight of cementitious materials. In some embodiments, the metakaolin may be present in an amount of about 1% to about 25% by weight of cementitious materials.


In certain embodiments, the cement compositions of the present invention further may comprise shale. Among other things, shale included in the cement compositions may react with excess lime to form a suitable cementing material, for example, calcium silicate hydrate. A variety of shales are suitable, including those comprising silicon, aluminum, calcium, and/or magnesium. An example of a suitable shale comprises vitrified shale. Suitable examples of vitrified shale include, but are not limited to, “PRESSUR-SEAL® FINE LCM” material and “PRESSUR-SEAL® COARSE LCM” material, which are commercially available from TXI Energy Services, Inc., Houston, Tex. Generally, the shale may have any particle size distribution as desired for a particular application. In certain embodiments, the shale may have a particle size distribution in the range of from about 37 micrometers to about 4,750 micrometers.


Where present, the shale may be included in the cement compositions of the present invention in an amount sufficient to provide the desired compressive strength, density, and/or cost. In some embodiments, the shale may be present in an amount of about 1% to about 75% by weight of cementitious materials. In some embodiments, the shale may be present in an amount of about 5% to about 35% by weight of cementitious materials. One of ordinary skill in the art, with the benefit of this disclosure, will recognize the appropriate amount of the shale to include for a chosen application.


In certain embodiments, the cement compositions of the present invention further may comprise zeolite. Zeolites generally are porous alumino-silicate minerals that may be either a natural or synthetic material. Synthetic zeolites are based on the same type of structural cell as natural zeolites, and may comprise aluminosilicate hydrates. As used herein, the term “zeolite” refers to all natural and synthetic forms of zeolite.


In certain embodiments, suitable zeolites for use in present invention may include “analcime” (which is hydrated sodium aluminum silicate), “bikitaite” (which is lithium aluminum silicate), “brewsterite” (which is hydrated strontium barium calcium aluminum silicate), “chabazite” (which is hydrated calcium aluminum silicate), “clinoptilolite” (which is hydrated sodium aluminum silicate), “faujasite” (which is hydrated sodium potassium calcium magnesium aluminum silicate), “ferrierite”, “harmotome” (which is hydrated barium aluminum silicate), “heulandite” (which is hydrated sodium calcium aluminum silicate), “laumontite” (which is hydrated calcium aluminum silicate), “mesolite” (which is hydrated sodium calcium aluminum silicate), “natrolite” (which is hydrated sodium aluminum silicate), “paulingite” (which is hydrated potassium sodium calcium barium aluminum silicate), “phillipsite” (which is hydrated potassium sodium calcium aluminum silicate), “scolecite” (which is hydrated calcium aluminum silicate), “stellerite” (which is hydrated calcium aluminum silicate), “stilbite” (which is hydrated sodium calcium aluminum silicate), and “thomsonite” (which is hydrated sodium calcium aluminum silicate), and combinations thereof. In certain embodiments, suitable zeolites for use in the present invention include chabazite and clinoptilolite. An example of a suitable source of zeolite is available from the C2C Zeolite Corporation of Calgary, Canada.


In some embodiments, the zeolite may be present in the cement compositions of the present invention in an amount of about 1% to about 65% by weight of cementitious materials. In certain embodiments, the zeolite may be present in an amount of about 1% to about 40% by weight of cementitious materials.


In addition, certain embodiments of the cement compositions may comprise nano-silica. The nano-silica may be described as particulate nano-silica. That is, the nano-silica may be particulate in nature and not, for example, a colloidal silica or a suspension of silica in solution. Indeed, in one embodiment, the particulate nano-silica may be added to the cement composition as a dry nano-silica powder. Generally, the particulate nano-silica may be defined as nano-silica having a mean particle size of less than or equal to about 100 nm. For example, the particulate nano-silica may have a mean particle size in the range of from about 1 nm to about 100 nm (about 1×10−9 m to about 100×10−9 m). In certain embodiments, the particulate nano-silica may have a particle size of less than or equal to about 50 nm. For example, the particulate nano-silica may have a particle size in the range of from about 5 nm to about 50 nm. In further certain embodiments, the particulate nano-silica may have a particle size of less than or equal to about 30 nm. For example, the particulate nano-silica may have a particle size in the range of from about 5 nm to about 30 nm. However, it should be noted that the particulate nano-silica may be utilized in combination with differently sized silica particles in accordance with present embodiments. For example, a number of silica particles with particle sizes greater than 100 nm may be included in a cement composition in accordance with present embodiments.


It is now recognized that the particulate nano-silica utilized with present embodiments, which may include silicon dioxide, may have an impact on certain physical characteristics of resulting cements. For example, relative to inclusion of colloidal silica or larger silica particles in a cement slurry, inclusion of particulate nano-silica in the cement slurry may provide improved mechanical properties, such as compressive strength, tensile strength, Young's modulus and Poisson's ratio. In addition, the particulate nano-silica also may be included in the cement composition as a set accelerator to accelerate the set time of the resultant cement composition. Accordingly, a cement composition in accordance with present embodiments may comprise a sufficient amount of particulate nano-silica to provide the desired characteristics in a resulting cement. In certain embodiments, the particulate nano-silica may be present in the cement composition in an amount in the range of from about 1% to about 25% by weight of cementitious materials. In certain embodiments, the particulate nano-silica may be present in the cement composition in an amount in the range of from about 5% to about 15% by weight of cementitious materials.


Other additives suitable for use in subterranean cementing operations also may be added to certain embodiments of the cement compositions. Examples of such additives include, strength-retrogression additives, set accelerators, weighting agents, weight-reducing additives, heavyweight additives, lost-circulation materials, filtration-control additives, dispersants, defoaming agents, foaming agents, and combinations thereof. Specific examples of these, and other, additives include crystalline silica, amorphous silica, salts, fibers, hydratable clays, vitrified shale, microspheres, lime, latex, thixotropic additives, combinations thereof and the like. A person having ordinary skill in the art, with the benefit of this disclosure, will readily be able to determine the type and amount of additive useful for a particular application and desired result.


As will be appreciated by those of ordinary skill in the art, certain embodiments of the cement compositions of the present invention may be used in a variety of subterranean applications, including primary and remedial cementing. Certain embodiments of the cement compositions may be introduced into a subterranean formation and allowed to set therein. Certain embodiments of the cement compositions may comprise nano-hydraulic cement, hydraulic cement, and water. By way of example, in certain primary cementing embodiments, a cement composition may be introduced into a space between a subterranean formation and a pipe string located in the subterranean formation. The cement composition may be allowed to set to form a hardened mass in the space between the subterranean formation and the pipe string. In addition, in certain remedial cementing embodiments, a cement composition may be used, for example, in squeeze-cementing operations or in the placement of cement plugs. For example, embodiments of the cement compositions may used to: penetrate a gravel pack to shut off water or gas production, penetrate a gravel pack to divert steam injections, and penetrate a gravel pack to plug and abandon a well. One or more hydrocarbons (e.g., oil, gas, etc.) may be produced from a well bore penetrating the subterranean formation.


While the preceding discussion is directed to the use of a non-hydraulic, particulate nano-silica and nano-hydraulic cement, those of ordinary skill in the art will also appreciate that it may be desirable to utilize other suitable types of non-hydraulic nano-particles, in accordance with embodiments of the present invention. Examples of such non-hydraulic nano-particles include nano-clays, nano-alumina, nano-zinc oxide, nano-boron, nano-iron oxide and combinations thereof. In certain embodiments, the nano-particles may be particulate in nature and not, for example, a colloidal nano-particle or a suspension of the nano-particle in solution. In certain embodiments, the nano-clay may comprise nano-montmorillonite. Nano-montmorillonite is member of the smectite-clay family, and belongs to the general mineral group of clays with a sheet-like structure where the dimensions in two directions far exceed its thickness. Generally, the nano-montmorillonite has of a three-layered structure of aluminum sandwiched between two layers of silicon, similar to the mica-type layered silicates. Montmorillonite is an active and major ingredient in a volcanic ash called bentonite, which has an ability to swell to many times its original weight and volume when it absorbs water. One example of a suitable nano-montmorillonite is NANOMER® nanoclay, which is available from Nanocor, Arlington Heights, Ill.


Furthermore, while the preceding discussion is directed to the use of nano-particles in well cementing methods, those of ordinary skill in the art will appreciate that the present technique also encompasses the use of nano-particles in any of a variety of different subterranean treatments. For example, nano-hydraulic cement may be included in any of a number of well treatment fluids that may be used in subterranean treatments, including drilling fluids, completion fluids, stimulation fluids and well clean-up fluids. In accordance with another embodiment, the nano-hydraulic cement may be included as proppant in a well treatment fluid. By way of example, a proppant may be used that comprises nano-hydraulic cement. In the proppant embodiments, the proppant comprising the nano-hydraulic cement may be prepared by a process comprising: allowing a cement composition comprising water, nano-hydraulic cement, and an optional hydraulic cement to set into a substantially hydrated mass; and comminuting the substantially hydrated mass into smaller particles so as to form the proppant (or substantially hydrated cement particles). The preparation of substantially hydrated cement particles is described in more detail in U.S. Pat. No. 6,648,962, the disclosure of which is incorporated herein by reference. When used as a proppant, for example, a well treatment fluid containing the proppant may be introduced into a subterranean formation at or above a fracturing pressure of a subterranean formation. At least a portion of the proppant may be deposited in one or more fractures in the subterranean formation such that the fractures are prevented from fully closing upon the release of pressure, forming conductive channels through which fluids may flow to (or from) the well bore.


In addition, the nano-particles may be also be used in gravel-packing operations. For example, particulates comprising nano-hydraulic cement may be used in a gravel-packing operation. A “gravel pack” is a term commonly use to refer to a volume of particulate materials (such as sand) placed into a well bore to at least partially reduce the migration of unconsolidated formation particulates into the well bore. The particulates for use in the gravel-packing operations may be prepared in a manner similar to the proppant comprising the nano-hydraulic cement. In gravel-packing embodiments, a volume of particulates comprising the nano-hydraulic cement may be placed in a gravel pack in a subterranean formation. In certain embodiments, a screen may be placed in the well bore and the annulus between the screen and the subterranean formation may be packed with the particulates. In certain embodiments, a screenless gravel-packing operation may be performed.


In addition to the use of the nano-particles without encapsulation, embodiments of the present invention may include using the nano-particles in a contained form. Among other things, use of contained nano-particles should facilitate their use in subterranean applications, for example, by alleviating potentially handling problems. In certain embodiments, contained nano-particles include encapsulated nano-particles. Specifically, encapsulation of the nano-particles in accordance with present embodiments may include enclosing the nano-particles within an outer coating or container in particulate form. Certain methods of encapsulation are set forth in U.S. Pat. Nos. 5,373,901; 6,444,316; 6,527,051; 6,554,071; 7,156,174; and 7,204,312, the disclosures of which are incorporated herein by reference.


Various types of encapsulation may be employed such that the nano-particles (e.g., the nano-hydraulic cement) are contained but retains its particulate nature and, thus, retains its corresponding impact on physical properties of cement slurries. For example, the nano-particles may be encapsulated within a bag, capsule, layer, coating or the like. Further, the material utilized to encapsulate the nano-particles may be selected to facilitate transportation and/or incorporation of the nano-particles into a well treatment fluid. For example, to facilitate handling of the nano-particles and/or to facilitate timed release of the nano-particles, the encapsulation material may be degradable. This may facilitate handling of the nano-particles by allowing inclusion of the encapsulated nano-particles in a well treatment fluid without requiring that the nano-particles first be removed from the encapsulating material. Further, the encapsulating material may be designed to degrade at a certain rate when in contact with certain materials (e.g., water) so that the nano-particles are released into the well treatment fluid at a desired time. Certain water-dissolvable materials that may be utilized to encapsulate the nano-particles are described in U.S. Pat. Nos. 4,961,790 and 5,783,541, the disclosures of which are incorporated herein by reference.


In accordance with certain embodiments, the cement compositions of the present invention may utilize a packing volume fraction suitable for a particular application as desired. As used herein, the term “packing volume fraction” refers to the volume of the particulate materials in a fluid divided by the total volume of the fluid. The size ranges of the preferred particulate materials are selected, as well as their respective proportions, in order to provide a maximized packing volume fraction so that the fluid is in a hindered settling state. It is known that, in such a state, the particulate materials behave “collectively” like a porous solid material. The hindered settling state is believed to correspond, in practice, to a much higher solid material concentration in the fluid than that present in the some traditional cement compositions.


The present embodiments may include a combination of at least three features to obtain a maximum packing volume fraction. One is the use of at least three particulate materials wherein the at least three particulate materials are in size ranges “disjointed” from one another. In some embodiments, each of the three particulate materials may include a different particle size selected from the following ranges: about 7 nm to about 50 nm, about 0.05 microns to about 0.5 microns, 0.5 microns to about 10 microns, about 10 microns to about 20 microns, about 20 microns to about 200 microns, about 200 microns to about 800 microns, and greater than about 1 millimeter. For example, a first particulate material may include particles sized from about 7 nm to about 50 nm, a second particulate material may include particles sized from about 0.05 microns to about 0.5 microns, and a third particulate material may include particles sized from about 10 microns to about 20 microns. In accordance with present embodiments, the first particulate material includes at least one of nano-hydraulic cement, nano-clay, nano-silica, nano-alumina, nano-zinc oxide, nano-boron, nano-iron oxide or combinations thereof. In certain embodiments, one or more of nano-hydraulic cement, micro-fine hydraulic cement, micro-fine slag, or other nano-particles may be used to maximize the packing volume fraction. Another feature of present embodiments may include a choice of the proportions of the three particulate materials in relation to the mixing, such that the fluid, when mixed, is in a hindered settling state. Another feature may include the choice of the proportions of the three particulate materials between each other, and according to their respective size ranges, such that the maximum packing volume fraction is at least substantially achieved for the sum total of all particulate materials in the fluid system. Packing volume fraction is described in further detail in U.S. Pat. No. 7,213,646, the disclosure of which is incorporated herein by reference.


In certain embodiments of the present invention, the nano-hydraulic cement composition described herein may be foamed using a gas and a foaming surfactant. The gas utilized in the foamed cement compositions of the present invention may be any gas suitable for foaming a cement composition, including, but not limited to, air or nitrogen, or combinations thereof. Generally, the gas should be present in the foamed cement compositions of the present invention in an amount sufficient to form a suitable foam. In certain embodiments, the gas may be present in an amount in the range of from about 10% and about 80% by volume of the composition.


Any suitable foaming and stabilizing surfactant may be used in the foamed cement composition of the present invention. Among other things, the foaming and stabilizing surfactants may facilitate the foaming of a cement composition and/or also stabilize the resultant foamed cement composition formed therewith. Suitable foaming and stabilizing surfactants may include, but are not limited to: mixtures of an ammonium salt of an alkyl ether sulfate, a cocoamidopropyl betaine surfactant, a cocoamidopropyl dimethylamine oxide surfactant, sodium chloride, and water; mixtures of an ammonium salt of an alkyl ether sulfate surfactant, a cocoamidopropyl hydroxysultaine surfactant, a cocoamidopropyl dimethylamine oxide surfactant, sodium chloride, and water; hydrolyzed keratin; mixtures of an ethoxylated alcohol ether sulfate surfactant, an alkyl or alkene amidopropyl betaine surfactant, and an alkyl or alkene dimethylamine oxide surfactant; aqueous solutions of an alpha-olefinic sulfonate surfactant and a betaine surfactant; and combinations thereof. An example of a suitable hydrolyzed keratin is described in U.S. Pat. No. 6,547,871, the disclosure of which is incorporated herein by reference. Example of suitable mixtures of an ethoxylated alcohol ether sulfate surfactant, an alkyl or alkene amidopropyl betaine surfactant, and an alkyl or alkene dimethylamine oxide surfactant is described in U.S. Pat. No. 6,063,738, the disclosure of which is incorporated herein by reference. Examples of suitable aqueous solutions of an alpha-olefinic sulfonate surfactant and a betaine surfactant are described in U.S. Pat. No. 5,897,699, the disclosure of which is incorporated herein by reference. In one embodiment, the foaming and stabilizing surfactant comprises a mixture of an ammonium salt of an alkyl ether sulfate, a cocoamidopropyl betaine surfactant, a cocoamidopropyl dimethylamine oxide surfactant, sodium chloride, and water.


Generally, the foaming and stabilizing surfactants should be present in the foamed cement compositions of the present invention in an amount sufficient to provide a suitable foam. In some embodiments, the foaming and stabilizing surfactant may be present in an amount in the range of from about 0.8% and about 5% by volume of the water present in the foamed cement composition.


Embodiments of the settable compositions of the present invention may also comprise swellable particles. As used herein, a particle is characterized as swelling when it swells upon contact with oil and/or an aqueous fluid (e.g., water). Swellable particles suitable for use in embodiments of the present invention may generally swell by up to about 50% of their original size at the surface. Under downhole conditions, this swelling may be more, or less, depending on the conditions presented. For example, the swelling may be at least 10% at downhole conditions. In some embodiments, the swelling may be up to about 50% under downhole conditions. However, as those of ordinary skill in the art, with the benefit of this disclosure, will appreciate, the actual swelling when the swellable particles are included in a settable composition may depend on, for example, the concentration of the swellable particles included in the settable composition. In accordance with embodiments of the present invention, the swellable particles may be included in the settable composition, for example, to counteract the formation of cracks in the cement sheath and/or micro-annulus between the cement sheath and the pipe string or the formation. In general, the swellable particles should be capable of swelling when contacted by aqueous fluids and/or oil to inhibit fluid flow through the crack and/or micro-annulus. Accordingly, the swellable particles may prevent and/or reduce the loss of zonal isolation in spite of the formation of cracks and/or micro-annulus, potentially resulting in an improved annular seal for the extended cement compositions.


An example of swellable particles that may be utilized in embodiments of the present invention comprises a swellable elastomer. Some specific examples of suitable swellable elastomers include, but are not limited to, natural rubber, acrylate butadiene rubber, polyacrylate rubber, isoprene rubber, chloroprene rubber, butyl rubber (IIR), brominated butyl rubber (BIIR), chlorinated butyl rubber (CIIR), chlorinated polyethylene (CM/CPE), neoprene rubber (CR), styrene butadiene copolymer rubber (SBR), sulphonated polyethylene (CSM), ethylene acrylate rubber (EAM/AEM), epichlorohydrin ethylene oxide copolymer (CO, ECO), ethylene-propylene rubber (EPM and EDPM), ethylene-propylene-diene terpolymer rubber (EPT), ethylene vinyl acetate copolymer, fluorosilicone rubbers (FVMQ), silicone rubbers (VMQ), poly 2,2,1-bicyclo heptene (polynorborneane), and alkylstyrene. One example of a suitable swellable elastomer comprises a block copolymer of a styrene butadiene rubber. Examples of suitable elastomers that swell when in contact with oil include, but are not limited to, nitrile rubber (NBR), hydrogenated nitrile rubber (HNBR, HNS), fluoro rubbers (FKM), perfluoro rubbers (FFKM), tetrafluorethylene/propylene (TFE/P), isobutylene maleic anhydride. Combinations of suitable swellable elastomers may also be used. Other swellable elastomers that behave in a similar fashion with respect to oil or aqueous fluids also may be suitable. Those of ordinary skill in the art, with the benefit of this disclosure, will be able to select an appropriate swellable elastomer for use in embodiments of the settable compositions of the present invention based on a variety of factors, including the application in which the composition will be used and the desired swelling characteristics.


An example of swellable particles that may be utilized in embodiments of the present invention comprises a water-swellable polymer. Some specific examples of suitable water-swellable polymers, include, but are not limited to starch-polyacrylate acid graft copolymer and salts thereof, polyethylene oxide polymer, carboxymethyl cellulose type polymers, polyacrylamide, poly(acrylic acid) and salts thereof, poly(acrylic acid-co-acrylamide) and salts thereof, graft-poly(ethylene oxide) of poly(acrylic acid) and salts thereof, poly(2-hydroxyethyl methacrylate), and poly(2-hydroxypropyl methacrylate). Combinations of suitable water-swellable polymers may also be used. In certain embodiments, the water-swellable polymers may be crosslinked and/or lightly crosslinked. Other water-swellable polymers that behave in a similar fashion with respect to aqueous fluids also may be suitable. Those of ordinary skill in the art, with the benefit of this disclosure, will be able to select appropriate water-swellable polymers for use in embodiments of the settable compositions of the present invention based on a variety of factors, including the application in which the composition will be used and the desired swelling characteristics.


Where used, the swellable particles generally may be included in the settable compositions in an amount sufficient to provide the desired mechanical properties. In some embodiments, the swellable particles may be present in the settable compositions in an amount up to about 25% by weight of the cementitious component. In some embodiments, the swellable particles may be present in the settable compositions in a range of about 5% to about 25% by weight of the cementitious component. In some embodiments, the swellable particles may be present in the settable compositions in a range of about 15% to about 20% by weight of the cementitious component.


In addition, the swellable particles that are utilized may have a wide variety of shapes and sizes of individual particles suitable for use in accordance with embodiments of the present invention. By way of example, the swellable particles may have a well-defined physical shape as well as an irregular geometry, including the physical shape of platelets, shavings, fibers, flakes, ribbons, rods, strips, spheroids, beads, pellets, tablets, or any other physical shape. In some embodiments, the swellable particles may have a particle size in the range of about 5 microns to about 1,500 microns. In some embodiments, the swellable particles may have a particle size in the range of about 20 microns to about 500 microns. However, particle sizes outside these defined ranges also may be suitable for particular applications.


Therefore, the present invention is well adapted to attain the ends and advantages mentioned as well as those that are inherent therein. The particular embodiments disclosed above are illustrative only, as the present invention may be modified and practiced in different but equivalent manners apparent to those skilled in the art having the benefit of the teachings herein. Furthermore, no limitations are intended to the details of construction or design herein shown, other than as described in the claims below. It is therefore evident that the particular illustrative embodiments disclosed above may be altered or modified and all such variations are considered within the scope and spirit of the present invention. In particular, every range of values (of the form, “from about a to about b,” or, equivalently, “from approximately a to b,” or, equivalently, “from approximately a-b”) disclosed herein is to be understood as referring to the power set (the set of all subsets) of the respective range of values, and set forth every range encompassed within the broader range of values. Also, the terms in the claims have their plain, ordinary meaning unless otherwise explicitly and clearly defined by the patentee.

Claims
  • 1. A method of cementing comprising: introducing a cement composition comprising nano-hydraulic cementitious particles, a hydraulic cement having a mean particle size greater of about 1 micron or greater, and water into a well bore, wherein the water is present in an amount between about 33% to about 200% of the cement composition, wherein the nano-hydraulic cementitious particles have a mean particle size of between about 20 nanometers to about 100 nanometers, the nano-hydraulic cementitious particles being selected from the group consisting of a Portland cement, a pozzolanic cement, a gypsum cement, a soil cement, a calcium phosphate cement, a high-alumina content cement, a silica cement, a high-alkalinity cement, and any combination thereof; andallowing the cement composition to set in the subterranean formation by reaction of the nano-hydraulic cementitious particles and the hydraulic cement with the water to form a hardened mass.
  • 2. The method of claim 1 wherein the nano-hydraulic cementitious particles comprise the pozzolanic cement.
  • 3. The method of claim 1 wherein the nano-hydraulic cementitious particles comprise the Portland cement.
  • 4. The method of claim 1 wherein the cement composition further comprises at least one nano-particle selected from the group consisting of nano-silica, nano-clay, nano-alumina, nano-zinc oxide, nano-boron, nano-iron oxide, and any combination thereof.
  • 5. The method of claim 1 wherein the cement composition further comprises a nano-clay.
  • 6. The method of claim 1 wherein the cement composition further comprises a swellable particle.
  • 7. The method of claim 1 wherein the cement composition further comprises micro-fine slag.
  • 8. The method of claim 1 wherein the cement composition further comprises micro-fine cement having a mean particle size of less than about 30 microns, but larger than 1 micron.
  • 9. The method of claim 1 wherein the cement composition further comprises cement kiln dust.
  • 10. The method of claim 1 wherein the cement composition further comprises at least one additive selected from the group consisting of fly ash, shale, slag, zeolite, metakaolin, and any combination thereof.
  • 11. The method of claim 1 wherein the cement composition is foamed.
  • 12. The method of claim 1 comprising maximizing a packing volume fraction in the cement composition.
  • 13. The method of claim 1 further comprising providing the nano-hydraulic cementitious particles, wherein at least of a portion of the nano-hydraulic cementitious particles as provided are contained or encapsulated in a degradable material.
  • 14. The method of claim 1 wherein the step of introduction is performed as part of remedial cementing.
  • 15. The method of claim 1 wherein the step of introduction is performed as part of squeeze cementing and the cement composition is placed in voids.
  • 16. The method of claim 1 wherein the voids are present in a pipe string, a cement sheath, a gravel pack, or a combination thereof.
  • 17. The method of claim 1 wherein the cement composition further comprises a swellable particle.
  • 18. The method of claim 1 wherein the swellable particle is present in an amount of about 5 weight percent to about 25 weight percent by combined weight of the nano-hydraulic cementitious particles and the hydraulic cement.
  • 19. The method of claim 17 wherein the swellable particle comprises a swellable elastomer.
  • 20. The method of claim 17 wherein the swellable particle is water swellable or oil swellable.
CROSS REFERENCE TO RELATED APPLICATION

The present application is a continuation of U.S. patent application Ser. No. 12/263,954, filed Nov. 3, 2008, entitled “Cement Compositions and Methods Utilizing Nano-Hydraulic Cement,” which is a continuation-in-part of U.S. patent application Ser. No. 11/388,645, filed Mar. 24, 2006, entitled “Subterranean Treatment Fluids Comprising Substantially Hydrated Cement Particulates,” now abandoned, which is a continuation-in-part of U.S. patent application Ser. No. 10/775,348, now U.S. Pat. No. 7,086,466, filed Feb. 10, 2004, entitled “Use of Substantially Hydrated Cement Particulates in Drilling and Subterranean Applications.” The present application is also a continuation-in-part of U.S. patent application Ser. No. 12/283,398, filed on Sep. 11, 2008, entitled “Settable Compositions Comprising Cement Kiln Dust and Swellable Particles,” which is a continuation-in-part of U.S. patent application Ser. No. 11/223,669, filed on Sep. 9, 2005, now U.S. Pat. No. 7,445,669, entitled “Settable Compositions Comprising Cement Kiln Dust and Additive(s).” The present application is also a continuation-in-part of U.S. patent application Ser. No. 11/747,002, filed on May 10, 2007, now U.S. Pat. No. 7,559,369, entitled “Well Treatment Compositions and Methods Utilizing Nano-Particles.” The entire disclosures of these applications are incorporated herein by reference.

US Referenced Citations (214)
Number Name Date Kind
2094316 Cross et al. Sep 1937 A
2329940 Ponzer Sep 1943 A
2842205 Allen et al. Jul 1958 A
2848051 Willaims Aug 1958 A
2871133 Palonen et al. Jan 1959 A
2945769 Gama et al. Jul 1960 A
3168139 Kennedy et al. Feb 1965 A
3454095 Messenger et al. Jul 1969 A
3499491 Wyant et al. Mar 1970 A
3557876 Tragesser Jan 1971 A
3748159 George Jul 1973 A
3876005 Fincher et al. Apr 1975 A
3887009 Miller et al. Jun 1975 A
3887385 Quist et al. Jun 1975 A
4018617 Nicholson Apr 1977 A
4031184 McCord Jun 1977 A
4176720 Wilson Dec 1979 A
4268316 Wills et al. May 1981 A
4341562 Ahlbeck Jul 1982 A
RE31190 Detroit et al. Mar 1983 E
4407677 Wills et al. Oct 1983 A
4432800 Kneller et al. Feb 1984 A
4435216 Diehl et al. Mar 1984 A
4460292 Durham et al. Jul 1984 A
4494990 Harris Jan 1985 A
4515635 Rao et al. May 1985 A
4519452 Tsao et al. May 1985 A
4555269 Rao et al. Nov 1985 A
4614599 Walker Sep 1986 A
4624711 Styron Nov 1986 A
4676317 Fry et al. Jun 1987 A
4741782 Styron May 1988 A
4761183 Clarke Aug 1988 A
4784223 Worrall et al. Nov 1988 A
4883125 Wilson et al. Nov 1989 A
4941536 Brothers et al. Jul 1990 A
4992102 Barbour Feb 1991 A
5030366 Wilson et al. Jul 1991 A
5049288 Brothers et al. Sep 1991 A
5058679 Hale et al. Oct 1991 A
RE33747 Hartley et al. Nov 1991 E
5086850 Harris et al. Feb 1992 A
5121795 Ewert et al. Jun 1992 A
5123487 Harris et al. Jun 1992 A
5125455 Harris et al. Jun 1992 A
5127473 Harris et al. Jul 1992 A
5149370 Olaussen et al. Sep 1992 A
5183505 Spinney Feb 1993 A
5213160 Nahm et al. May 1993 A
5238064 Dahl et al. Aug 1993 A
5266111 Barbour Nov 1993 A
5295543 Terry et al. Mar 1994 A
5305831 Nahm Apr 1994 A
5314022 Cowan et al. May 1994 A
5327968 Onan et al. Jul 1994 A
5337824 Cowan Aug 1994 A
5346012 Heathman et al. Sep 1994 A
5352288 Mallow Oct 1994 A
5358044 Hale et al. Oct 1994 A
5358049 Hale et al. Oct 1994 A
5361841 Hale et al. Nov 1994 A
5361842 Hale et al. Nov 1994 A
5368103 Heathman et al. Nov 1994 A
5370185 Cowan et al. Dec 1994 A
5372641 Carpenter Dec 1994 A
5382290 Nahm et al. Jan 1995 A
5383521 Onan et al. Jan 1995 A
5383967 Chase Jan 1995 A
5398758 Onan et al. Mar 1995 A
5423379 Hale et al. Jun 1995 A
5439056 Cowan Aug 1995 A
5458195 Totten et al. Oct 1995 A
5464060 Hale et al. Nov 1995 A
5472051 Brothers Dec 1995 A
5476144 Nahm et al. Dec 1995 A
5484019 Griffith Jan 1996 A
5494513 Fu et al. Feb 1996 A
5499677 Cowan Mar 1996 A
5515921 Cowan et al. May 1996 A
5518996 Maroy et al. May 1996 A
5520730 Barbour May 1996 A
5529624 Riegler Jun 1996 A
5536311 Rodrigues Jul 1996 A
5542782 Carter et al. Aug 1996 A
5569324 Totten et al. Oct 1996 A
5571318 Griffith et al. Nov 1996 A
5580379 Cowan Dec 1996 A
5585333 Dahl et al. Dec 1996 A
5588489 Chatterji et al. Dec 1996 A
5673753 Hale et al. Oct 1997 A
5711383 Terry et al. Jan 1998 A
5716910 Totten et al. Feb 1998 A
5728654 Dobson et al. Mar 1998 A
5851960 Totten et al. Dec 1998 A
5866516 Costin Feb 1999 A
5874387 Carpenter et al. Feb 1999 A
5897699 Chatterji et al. Apr 1999 A
5900053 Brothers et al. May 1999 A
5913364 Sweatman Jun 1999 A
5988279 Udarbe et al. Nov 1999 A
6022408 Stokes et al. Feb 2000 A
6060434 Sweatman et al. May 2000 A
6060535 Villar et al. May 2000 A
6063738 Chatterji et al. May 2000 A
6138759 Chatterji et al. Oct 2000 A
6143069 Brothers et al. Nov 2000 A
6145591 Boncan et al. Nov 2000 A
6153562 Villar et al. Nov 2000 A
6167967 Sweatman Jan 2001 B1
6170575 Reddy et al. Jan 2001 B1
6230804 Mueller et al. May 2001 B1
6244343 Brothers et al. Jun 2001 B1
6245142 Reddy et al. Jun 2001 B1
6258757 Sweatman et al. Jul 2001 B1
6277189 Chugh Aug 2001 B1
6312515 Barlet-Gouedard et al. Nov 2001 B1
6315042 Griffith et al. Nov 2001 B1
6332921 Brothers et al. Dec 2001 B1
6367550 Chatterji et al. Apr 2002 B1
6379456 Heathman et al. Apr 2002 B1
6402833 O'Hearn et al. Jun 2002 B1
6409819 Ko Jun 2002 B1
6457524 Roddy Oct 2002 B1
6478869 Reddy et al. Nov 2002 B2
6488763 Brothers et al. Dec 2002 B2
6494951 Reddy et al. Dec 2002 B1
6500252 Chatterji et al. Dec 2002 B1
6508305 Brannon et al. Jan 2003 B1
6524384 Griffith et al. Feb 2003 B2
6547871 Chatterji et al. Apr 2003 B2
6547891 Linden et al. Apr 2003 B2
6561273 Brothers et al. May 2003 B2
6562122 Dao et al. May 2003 B2
6565644 Kepler et al. May 2003 B2
6565647 Day et al. May 2003 B1
6572697 Gleeson et al. Jun 2003 B2
6610139 Reddy et al. Aug 2003 B2
6626243 Go Boncan Sep 2003 B1
6645290 Barbour Nov 2003 B1
6656265 Garnier et al. Dec 2003 B1
6660080 Reddy et al. Dec 2003 B2
6666268 Griffith et al. Dec 2003 B2
6668929 Griffith et al. Dec 2003 B2
6689208 Brothers Feb 2004 B1
6702044 Reddy et al. Mar 2004 B2
6706108 Polston Mar 2004 B2
6716282 Griffith et al. Apr 2004 B2
6729405 DiLullo et al. May 2004 B2
6767398 Trato Jul 2004 B2
6776237 Dao et al. Aug 2004 B2
6796378 Reddy et al. Sep 2004 B2
6797054 Chatterji et al. Sep 2004 B2
6823940 Reddy et al. Nov 2004 B2
6835243 Brothers et al. Dec 2004 B2
6837316 Reddy et al. Jan 2005 B2
6846357 Reddy et al. Jan 2005 B2
6848519 Reddy et al. Feb 2005 B2
6874578 Garnier Apr 2005 B1
6887833 Brothers et al. May 2005 B2
6889767 Reddy et al. May 2005 B2
6904971 Brothers et al. Jun 2005 B2
6908508 Brothers Jun 2005 B2
6911078 Barlet-Gouedard et al. Jun 2005 B2
7048053 Santra et al. May 2006 B2
7077203 Roddy et al. Jul 2006 B1
7156174 Roddy et al. Jan 2007 B2
7174962 Roddy et al. Feb 2007 B1
7199086 Roddy et al. Apr 2007 B1
7204307 Roddy et al. Apr 2007 B2
7204310 Roddy et al. Apr 2007 B1
7213646 Roddy et al. May 2007 B2
7284609 Roddy et al. Oct 2007 B2
7335252 Roddy et al. Feb 2008 B2
7337842 Roddy et al. Mar 2008 B2
7353870 Roddy et al. Apr 2008 B2
7381263 Roddy et al. Jun 2008 B2
7387675 Roddy et al. Jun 2008 B2
20020033121 Marko Mar 2002 A1
20020073897 Trato Jun 2002 A1
20020117090 Ku Aug 2002 A1
20030116065 Griffith et al. Jun 2003 A1
20030116887 Scott Jun 2003 A1
20030167970 Polston Sep 2003 A1
20040007162 Morioka et al. Jan 2004 A1
20040040475 De La Roij et al. Mar 2004 A1
20040079260 Datta et al. Apr 2004 A1
20040107877 Getzlaf et al. Jun 2004 A1
20040108113 Luke et al. Jun 2004 A1
20040112600 Luke et al. Jun 2004 A1
20040187740 Timmons Sep 2004 A1
20040188091 Luke et al. Sep 2004 A1
20040191439 Bour et al. Sep 2004 A1
20040211562 Brothers et al. Oct 2004 A1
20040211564 Brothers et al. Oct 2004 A1
20040244650 Brothers Dec 2004 A1
20040244977 Luke et al. Dec 2004 A1
20040256102 Trato Dec 2004 A1
20050000734 Getzlaf et al. Jan 2005 A1
20050034867 Griffith et al. Feb 2005 A1
20050056191 Brothers et al. Mar 2005 A1
20050072599 Luke et al. Apr 2005 A1
20050084334 Shi et al. Apr 2005 A1
20050098317 Reddy et al. May 2005 A1
20050133221 Chatterji et al. Jun 2005 A1
20060025312 Santra et al. Feb 2006 A1
20060162926 Roddy Jul 2006 A1
20060166834 Roddy Jul 2006 A1
20060260512 Nordmeyer Nov 2006 A1
20070056475 Roddy et al. Mar 2007 A1
20070056479 Gray Mar 2007 A1
20070056733 Roddy et al. Mar 2007 A1
20070186820 O'Hearn Aug 2007 A1
20080277116 Roddy et al. Jan 2008 A1
20080156491 Roddy et al. Jul 2008 A1
Foreign Referenced Citations (18)
Number Date Country
2153372 Jan 2006 CA
0814067 Dec 1997 EP
1236701 Sep 2002 EP
1394137 Jul 2003 EP
1348831 Oct 2003 EP
1469954 Apr 1997 GB
52117316 Oct 1977 JP
10110487 Apr 1998 JP
MXA2009000328 Jan 2009 MX
1373781 Feb 1988 SU
WO 8301443 Sep 1982 WO
WO 9854108 Dec 1998 WO
WO 0063134 Jan 2000 WO
WO 0050357 Aug 2000 WO
WO 03031364 Apr 2003 WO
WO 2005047212 May 2005 WO
WO 2005061846 Jul 2005 WO
WO 2005087660 Sep 2005 WO
Non-Patent Literature Citations (108)
Entry
U.S. Appl. No. 12/263,954, filed Nov. 3, 2008, Roddy.
U.S. Appl. No. 12/264,010, filed Nov. 3, 2008, Roddy.
U.S. Appl. No. 12/283,398, filed Sep. 11, 2008, Roddy.
Bartlet-Gouedard, “A Non-Conventional Way of Developing Cement Slurry for Geothermal Wells”, 2001.
Poon, “A Study of the Hydration of Natural Zeolite Blended Cement Pastes”, 1999.
“Beneficial use of Solid Waste in Maine”Apr. 14, 2005.
Smith, “Cementing” Society of Petroleum Engineers, p. 38, 1990.
Smith, “Cementing” Society of Professional Engineers, pp. 14, 38, 1987.
Chan, Comparative Study of the Initial Surface Absorption and Chloride Diffusion of High Performance Zeolite Silica Fume and PFA concretes, 1999.
Rogers, “Designing a Remedial Acid Treatment for Gulf of Mexico Deepwater Turbidite Sands Containing Zeolite Cement”, 1996.
Janotka, “Effect of Bentonite and Zeolite on Durability of Cement Suspension Under Sulfate Attack”, 1998.
Ding, “Extreme Vertices Design of Concrete With Combined Mineral Admixtures”, 1999.
“Kiln Dusts”, Apr. 14, 2005.
Sersale, “Portland-Zeolite-Cement for Minimizing Alkali-Aggregate Expansion”, 1987.
“Standards for the Management of Cement Kiln Dust Waste”, Apr. 14, 2005.
Naiqian, “Study on the Suppression Effect of Natural Zeolite on Expansion of Concrete Due to Alkali-Aggregate Reaction”, 1998.
Janotka, “The Properties of Mortar Using Blends With Portland Cement Clinker, Zeolite Tuff and Gypsum”, 1995.
Herndon, “Setting Downhole Plugs: A State-of-the-Art, Petroleum Engineer International”, Apr. 1978.
Sugama, “Carbonation of Hydrothermally Treated Phosphate-Bonded Calcium Aluminate Cements”, pp. 1-9.
Sugama, “Hot Alkali Carbonation of Sodium Metaphosphate Modified Fly Ash/Calcium Aluminate Blend Hydrothermal Cements”, pp. 1661-1672, Sep. 11, 1996.
“Use of Cement Kiln Dust for the Stabilization of Soils”, R. L. Parsons, et al., Apr. 14, 2005.
Feng, “Zeolite Ceramiste Cellular Concrete”, 2000.
Marfil, “Zeolite Crystallization in Portland Cement Concrete Due to Alkali-Aggregate Reaction”, 1993.
Atkins, “Zeolite P in Cements”, “Its Potential for Immobilizing Toxic and Radioactive Waste Species”, 1995.
HES Brochure “AQF-2 Foaming Agent”, 1999.
HES Brochure “Halad-23 Fluid Loss Additive”, 2000.
HES Brochure “Halad-344 Fluid Loss Additive”, 1998.
HES Brochure “Halad-413 Fluid Loss Additive”, 1999.
HES Brochure “Howco Suds Surfactant”, 1999.
HES Brochure “HR-12 Cement Retarder”, 1999.
HES Brochure “HR-15 Cement Retarder”, 1999.
HES Brochure “HR-25 Cement Retarder” dated 1999.
HES Brochure “HR-4 Cement Retarder”, 1999.
HES Brochure HR-5 Cement Additive, 1998.
HES Brochure “HR-7 Cement Retarder”, 1999.
HES Brochure “Pozmix A Cement Additive”, 1999.
HES Brochure “Pozmix Cement and Pozmix 140”.
HES Brochure “SCR-100 Cement Retarder A Valuable Time Saver”, 1994.
HES Brochure “SCR-100 Cement Retarder”, 1999.
HES Brochure “SCR-500L High Temp Retarder”, 2000.
HES Brochure “ThermaLock™ Cement for Corrosive CO2 Environments”, 1999.
“3M Scotchlite, Glass Bubbles Floated Product Series Product Information”, 1999.
“API Specification for Materials and Testing for Well Cements”, API Spec. 10, 5th ed., pp. 7, 19-21, Jul. 1, 1980.
“Appendix A”, API RP 13B-2, 2d ed.; pp. 6-8, Dec. 1, 1991.
LAFARGE brochure “TerraCem™”, Aug. 2006.
LAFARGE MSDS “Cement Kiln Dust”, Mar. 3, 2005.
LAFARGE MSDS “LaFarge Blended Cement (cement)”, Mar. 3, 2005.
TXI Material Safety Data Sheet for Pressur-Seal, Oct. 2003.
“Manufacture of supplementary cementitious materials from cement kiln dust”, Mishulovich et al., World Cement Research and Development, p. 116-120, Mar. 1996.
“Alkali-activated binders by use of industrial by-products”, Buchwald et al., Cement and concrete Research 35, p. 968-793, 2005.
Answer 13 of 24 Chemical Abstracts on STN “Manufacture of ceramic particles from floatstone and fly ash”, CN 1182062 (abstract only).
Answer 3 of 24 Chemical Abstracts on STN “Effect of cement kiln dust substitution on chemical and physical properties and compressive strength of Portland and slag cements”, Adb El-aleem et al. (abstract only), 2005.
Office Action from U.S. Appl. No. 11/223,671, dated Dec. 15, 2005.
Office Action from U.S. Appl. No. 11/271,431, dated Mar. 6, 2006.
Office Action from U.S. Appl. No. 11/223,671, dated Mar. 31, 2006.
Office Action from U.S. Appl. No. 11/271,431, dated May 17, 2006.
Office Action from U.S. Appl. No. 11/271,431 (Advisory Action), dated Jul. 11, 2006.
Office Action from U.S. Appl. No. 11/416,563, dated Jul. 21, 2006.
Office Action from U.S. Appl. No. 11/403,032, dated Jul. 24, 2006.
Office Action from U.S. Appl. No. 11/271,431, dated Aug. 15, 2006.
Office Action from U.S. Appl. No. 11/440,627, dated Aug. 21, 2006.
Office Action from U.S. Appl. No. 11/402,741, dated Oct. 19, 2006.
Office Action from U.S. Appl. No. 11/484,951, dated Oct. 26, 2006.
Office Action from U.S. Appl. No. 11/484,951, dated Dec. 21, 2006.
Office Action from U.S. Appl. No. 11/223,703, dated Jan. 17, 2007.
Office Action from U.S. Appl. No. 11/402,741, dated Feb. 2, 2007.
Office Action from U.S. Appl. No. 11/223,485, dated Feb. 28, 2007.
Office Action from U.S. Appl. No. 11/223,669, dated Feb. 28, 2007.
Office Action from U.S. Appl. No. 11/271,690, dated Mar. 13, 2007.
Office Action from U.S. Appl. No. 11/402,741, dated Mar. 22, 2007.
Office Action from U.S. Appl. No. 11/223,703, dated Apr. 25, 2007.
Office Action from U.S. Appl. No. 11/402,741, dated May 29, 2007.
Office Action from U.S. Appl. No. 11/223,669, dated Jun. 18, 2007.
Office Action from U.S. Appl. No. 11/416,754 (Notice of Allowance), dated Jul. 2, 2007.
Office Action from U.S. Appl. No. 11/223,485 (Notice of Allowance), dated Aug. 3, 2007.
Office Action from U.S. Appl. No. 11/257,261, dated Aug. 10, 2007.
Office Action from U.S. Appl. No. 11/271,690 (Notice of Allowance), dated Aug. 13, 2007.
Office Action from U.S. Appl. No. 11/402,741, dated Sep. 6, 2007.
Office Action from U.S. Appl. No. 11/223,669, dated Oct. 9, 2007.
Office Action from U.S. Appl. No. 11/223,750, dated Oct. 16, 2007.
Office Action from U.S. Appl. No. 11/416,754 (Notice of Allowance), dated Oct. 17, 2007.
Office Action from U.S. Appl. No. 11/257,261 (Notice of Allowance), dated Oct. 23, 2007.
Office Action from U.S. Appl. No. 11/402,741, dated Oct. 24, 2007.
Office Action from U.S. Appl. No. 11/223,750 (Notice of Allowance), dated Dec. 11, 2007.
Office Action from U.S. Appl. No. 11/402,741 (Notice of Allowance), dated Dec. 13, 2007.
Office Action from U.S. Appl. No. 11/223,669, dated Jan. 29, 2008.
Office Action from U.S. Appl. No. 11/256,824 (Notice of Allowance), dated Feb. 27, 2008.
Office Action from U.S. Appl. No. 11/223,703 (Notice of Allowance), dated Feb. 27, 2008.
Office Action from U.S. Appl. No. 11/223,669, dated Apr. 8, 2008.
Office Action from U.S. Appl. No. 11/223,669 (Notice of Allowance), dated Jun. 30, 2008.
Foreign Search Report from a Related Application, dated Sep. 9, 2005.
Foreign Search Report from a Related Application, dated Jun. 5, 2006.
Foreign Search Report from a Related Application, dated Oct. 27, 2006.
Foreign Search Report from a Related Application, dated Nov. 2, 2006.
Foreign Search Report from a Related Application, dated Dec. 1, 2006.
Foreign Search Report from a Related Application, dated Dec. 19, 2006.
Foreign Search Report from a Related Application, dated May 8, 2007.
Office Action from U.S. Appl. No. 12/034,886 (Notice of Allowance), dated Oct. 21, 2008.
Harris et al. “Successful Remedial Operations Using Ultrafine Cement” SPE 24294, 1992.
Heathman et al. “Case Histories Regarding the Application of Microfine Cements” Cementing Technical Paper SPE 23926, 1992.
Halliburton brochure entitled “Micro Matrix Cement”, Nov. 2006.
Dalrymple et al. “A Selective Water Control Process” SPE 24330, 1992.
Halim et al. “Preparation of an ultra fast binding cement from calcium silicate-based mixed oxide nanoparticles” Nanotechnology 18, 2007.
Epik Energy brochure entitled “Nanocement”.
Nanocor brochure entitled “Nanoclay Structure”, Jun. 24, 2008.
He et al. “Chloride Permeability and Microstructure of Portland Cement Mortars Incorporating Nanomaterials” Abstract, Transportation Research Board Annual Meeting 2007 Paper #08-1041, 2008.
Chang et al. “Material properties of portland cement paste with nano-montmorillonite” J Mater Sci (2007), May 18, 2007.
Mexican Office Action for Application No. Mx/a/2014/014121 dated Mar. 23, 2018.
Related Publications (1)
Number Date Country
20170073568 A1 Mar 2017 US
Continuations (1)
Number Date Country
Parent 12263954 Nov 2008 US
Child 15339277 US
Continuation in Parts (6)
Number Date Country
Parent 11388645 Mar 2006 US
Child 12263954 US
Parent 10775348 Feb 2004 US
Child 11388645 US
Parent 12263954 US
Child 11388645 US
Parent 12283398 Sep 2008 US
Child 12263954 US
Parent 11223669 Sep 2005 US
Child 12283398 US
Parent 11747002 May 2007 US
Child 12263954 US