Compositions comprising kiln dust and wollastonite and methods of use in subterranean formations

Information

  • Patent Grant
  • 9157020
  • Patent Number
    9,157,020
  • Date Filed
    Wednesday, November 13, 2013
    10 years ago
  • Date Issued
    Tuesday, October 13, 2015
    8 years ago
Abstract
Embodiments relate to cementing operations and, more particularly, in certain embodiments, to settable compositions that comprise kiln dust and wollastonite and methods of use in subterranean formations. An embodiment discloses a method of cementing comprising: providing a settable composition comprising kiln dust, wollastonite, and water; and allowing the settable composition to set.
Description
BACKGROUND

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.


In cementing methods, such as well construction and remedial cementing, settable compositions are commonly utilized. As used herein, the term “settable composition” refers to a composition(s) that hydraulically sets or otherwise develops compressive strength. Settable compositions may be used in primary cementing operations whereby pipe strings, such as casing and liners, are cemented in well bores. In performing primary cementing, a settable composition may be pumped into an annulus between a subterranean formation and the pipe string disposed in the subterranean formation. The settable composition should set in the annulus, thereby forming an annular sheath of hardened cement (e.g., a cement sheath) that should support and position the pipe string in the well bore and bond the exterior surface of the pipe string to the walls of the well bore. Settable compositions also may be used in remedial cementing methods, such as the placement of cement plugs, and in squeeze cementing for sealing voids in a pipe string, cement sheath, gravel pack, formation, and the like. Settable compositions may also be used in surface applications, for example, construction cementing.


Settable compositions for use in subterranean formations may further include Portland cement. Portland cement generally is a major component of the cost for the settable compositions. Other components may be included in the settable composition in addition to, or in place of, the Portland cement. Such components may include fly ash, slag, shale, zeolite, metakaolin, pumice, perlite, lime, silica, rice-hull ash, micro-fine cement, lime kiln dust, and the like. However, the operating conditions for wells are becoming more challenging and demanding, and the search for new materials continues to meet these challenges.





BRIEF DESCRIPTION OF THE DRAWINGS

These drawings illustrate certain aspects of some of the embodiments of the present invention, and should not be used to limit or define the invention.



FIG. 1 illustrates a system for preparation and delivery of a settable composition to a well bore in accordance with certain embodiments.



FIG. 2A illustrates surface equipment that may be used in placement of a settable composition in a well bore in accordance with certain embodiments.



FIG. 2B illustrates placement of a settable composition into a well bore annulus in accordance with certain embodiments.





DESCRIPTION OF PREFERRED EMBODIMENTS

Embodiments relate to cementing operations and, more particularly, in certain embodiments, to settable compositions that comprise kiln dust and wollastonite and methods of use in subterranean formations. In some embodiments, the settable compositions may comprise kiln dust, wollastonite, and water. One of the many potential advantages of particular embodiments is that the inclusion of the wollastonite in embodiments of the settable compositions may increase the strength of the resultant set composition. Another potential advantage of some embodiments is that the kiln dust, wollastonite, or a combination thereof may be used to reduce the amount of a higher cost component, such as Portland cement, resulting in a more economical settable composition. Yet another potential advantage of some embodiments is that reduction of the amount of Portland cement can reduce the carbon footprint of the cementing operation.


Embodiments of the settable compositions may comprise kiln dust. Kiln dust, as that term is used herein, refers to a solid material generated as a by-product of the heating of certain materials in kilns. The term “kiln dust” as used herein is intended to include kiln dust made as described herein and equivalent forms of kiln dust. Kiln dust typically exhibits cementitious properties in that can set and harden in the presence of water. Examples of suitable kiln dusts include cement kiln dust, lime kiln dust, and combinations thereof. Cement kiln dust may be generated as a by-product of cement production that is removed from the gas stream and collected, for example, in a dust collector. Usually, large quantities of cement kiln dust are collected in the production of cement that are commonly disposed of as waste. Disposal of the cement kiln dust can add undesirable costs to the manufacture of the cement, as well as the environmental concerns associated with its disposal. The chemical analysis of the cement kiln dust from various cement manufactures varies depending on a number of factors, including the particular kiln feed, the efficiencies of the cement production operation, and the associated dust collection systems. Cement kin dust generally may comprise a variety of oxides, such as SiO2, Al2O3, Fe2O3, CaO, MgO, SO3, Na2O, and K2O. Problems may also be associated with the disposal of lime kiln dust, which may be generated as a by-product of the calcination of lime. The chemical analysis of lime kiln dust from various lime manufacturers varies depending on a number of factors, including the particular limestone or dolomitic limestone feed, the type of kiln, the mode of operation of the kiln, the efficiencies of the lime production operation, and the associated dust collection systems. Lime kiln dust generally may comprise varying amounts of free lime and free magnesium, lime stone, and/or dolomitic limestone and a variety of oxides, such as SiO2, Al2O3, Fe2O3, CaO, MgO, SO3, Na2O, and K2O, and other components, such as chlorides.


The kiln dust may be included in the settable compositions in an amount sufficient to provide, for example, the desired compressive strength, among other properties. In some embodiments, the kiln dust may be present in the settable compositions in an amount in the range of from about 1% to about 99% by weight of cementitious components (“% bwoc”). The term “cementitious components” refers to the components, or a combination thereof, of the settable compositions that hydraulically set, or otherwise harden, to develop compressive strength, including, for example, kiln dust, Portland cement, fly ash, natural pozzolans (e.g., pumice), slag, vitrified shale, metakaolin, rice husk ash, and the like. The cementitious components in some embodiments may be present in the settable composition in an amount of from about 25% to about 75% by weight of the settable composition. The kiln dust may be present in an amount, for example, ranging between any of and/or including any of about 5%, about 10%, about 15%, about 20%, about 25%, about 30%, about 35%, about 40%, about 45%, about 50%, about 55%, about 60%, about 65%, about 70%, about 75%, about 80%, or about 90% bwoc. In specific embodiments, the kiln dust may be present in the settable compositions in an amount in the range of from about 5% to 90% bwoc, from about 20% to about 50%, or from about 20% to about 30% bwoc. One of ordinary skill in the art, with the benefit of this disclosure, should recognize the appropriate amount of the kiln dust to include for a chosen application.


In some embodiments, the settable compositions may comprise wollastonite. Wollastonite is generally a calcium inosilicate mineral used in industrial applications, such as ceramics, friction products, metal making, paint filler, and plastics. Wollastonite may be mined in a number of different locations throughout the world and then processed for use in industrial applications. Wollastonite may be considered a cementitious component as can set and harden in the presence of silica, lime and water. The wollastonite used in some embodiments may have a mean particle size in a range of from about 1 micron to about 200 microns, and, alternatively, from about 5 microns to about 100 microns. The wollastonite may be included in embodiments of the settable compositions in an amount suitable for a particular application. In some embodiments, the wollastonite may be present in the settable compositions in an amount in a range of from about 1% to about 75% bwoc. In particular embodiments, the wollastonite may be present in an amount ranging between any of and/or including any of 5%, about 10%, about 15%, about 20%, about 25%, about 30%, about 35%, about 40%, about 45%, about 50%, about 55%, about 60%, about 65%, about 70%, or about 75% bwoc. In specific embodiments, wollastonite may be present in the settable compositions in an amount in the range of from about 5% to 50% bwoc or from about 20% to about 30% bwoc. One of ordinary skill, with the benefit of this disclosure, should recognize the amount of the wollastonite to include for a chosen application.


The water used in embodiments of the settable compositions may include, for example, freshwater, saltwater (e.g., water containing one or more salts dissolved therein), brine (e.g., saturated saltwater produced from subterranean formations), seawater, or any combination thereof. Generally, the water may be from any source, provided, for example, that it does not contain an excess of compounds that may undesirably affect other components in the settable composition. In some embodiments, the water may be included in an amount sufficient to form a pumpable slurry. In some embodiments, the water may be included in the settable compositions in an amount in a range of from about 40% to about 200% bwoc. In some embodiments, the water may be included in an amount in a range of from about 40% to about 150% bwoc.


In some embodiments, the settable compositions may further comprise a Portland cement, including, but not limited to, those classified as Class A, C, G and H cements according to American Petroleum Institute, API Specification for Materials and Testing for Well Cements, API Specification 10, Fifth Ed., Jul. 1, 1990. In addition, in some embodiments, Portland cements suitable for use in some embodiments may be classified as ASTM Type I, II, or III. Where present, the Portland cement generally may be included in the settable compositions in an amount sufficient to provide the desired compressive strength, density, and/or cost. In some embodiments, the Portland cement may be present in the settable compositions in an amount in the range of from about 1% to about 75% bwoc. For example, the hydraulic cement may be present in an amount ranging between any of and/or including any of about 1%, about 5%, about 10%, about 20%, about 30%, about 40%, about 50%, about 60%, about 70%, or about 75% bwoc.


Other optional additives may be included in embodiments of the settable compositions, including, but not limited to, fly ash, slag, shale (e.g., vitrified shale), zeolite, metakaolin, pumice, perlite, lime, silica (e.g., amorphous silica, crystalline silica), rice husk ash, small-particle size cement, and combinations thereof. As used herein, the term “small-particle size cement” refers to a cement having a particle size (or d50) no larger than about 5 microns, for example, in a range of about 1 micron to about 5 microns. Where present, these optional additives individually may be included in the settable compositions in an amount in a range of from about 0.1% to about 90% bwoc. For example, one or more of the optional additives may be individually be included in an amount ranging between any of and/or including any of about 5%, about 10%, about 15%, about 20%, about 25%, about 30%, about 35%, about 40%, about 45%, about 50%, about 55%, about 60%, about 65%, about 70%, about 75%, about 80%, about 85%, or about 90% bwoc. One of ordinary skill in the art, with the benefit of this disclosure, will recognize the appropriate amount of the optional to include for a chosen application.


Other additives suitable for use in cementing operations may also be added to embodiments of the settable compositions as desired for a particular application. Examples of such additives include, but are not limited to, dispersants, strength-retrogression additives, set accelerators, set retarders, weighting agents, lightweight additives, gas-generating additives, mechanical property enhancing additives, lost-circulation materials, fluid loss control additives, foaming agents, defoaming agents, oil-swellable particles, water-swellable particles, thixotropic additives, and any combination thereof. Specific examples of these, and other, additives include crystalline silica, fumed silica, silicates, salts, fibers, hydratable clays, microspheres, diatomaceous earth, elastomers, elastomeric particles, resins, latex, any combination 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.


Dispersants may be included in embodiments of the settable compositions. Where present, the dispersant should act, among other things, to control the rheology of the settable composition. While a variety of dispersants known to those skilled in the art may be used in some embodiments, examples of suitable dispersants include naphthalene sulfonic acid condensate with formaldehyde; acetone, formaldehyde, and sulfite condensate; melamine sulfonate condensed with formaldehyde; any combination thereof.


Strength-retrogression additives may be included in embodiments of the settable composition to, for example, prevent the retrogression of strength after the settable composition has been allowed to develop compressive strength when the settable composition is exposed to high temperatures. These additives may allow the settable compositions to form as intended, preventing cracks and premature failure of the cementitious composition. Examples of suitable strength-retrogression additives may include, but are not limited to, amorphous silica, coarse grain crystalline silica, fine grain crystalline silica, or a combination thereof.


Set accelerators may be included in embodiments of the settable compositions to, for example, increase the rate of setting reactions. Control of setting time may allow for the ability to adjust to well bore conditions or customize set times for individual jobs. Examples of suitable set accelerators may include, but are not limited to, aluminum sulfate, alums, calcium chloride, calcium sulfate, gypsum-hemihydrate, sodium aluminate, sodium carbonate, sodium chloride, sodium silicate, sodium sulfate, ferric chloride, or a combination thereof.


Set retarders may be included in embodiments of the settable compositions to, for example, increase the thickening time of the settable compositions. Examples of suitable set retarders include, but are not limited to, ammonium, alkali metals, alkaline earth metals, borax, metal salts of calcium lignosulfonate, carboxymethyl hydroxyethyl cellulose, sulfoalkylated lignins, hydroxycarboxy acids, copolymers of 2-acrylamido-2-methylpropane sulfonic acid salt and acrylic acid or maleic acid, saturated salt, or a combination thereof One example of a suitable sulfoalkylated lignin comprises a sulfomethylated lignin.


Weighting agents may be included in embodiments of the settable compositions to, for example, increase the density of the settable compositions. Examples of suitable weighting agents include, but not limited to, ground barium sulfate, barite, hematite, calcium carbonate, siderite, llmenite, manganese oxide, sand, salt, or a combination thereof.


Lightweight additives may be included in embodiments of the settable compositions to, for example, decrease the density of the settable compositions. Examples of suitable lightweight additives include, but are not limited to, bentonite, coal, diatomaceous earth, expanded perlite, fly ash, gilsonite, hollow microspheres, low-density elastic beads, nitrogen, pozzolan-bentonite, sodium silicate, combinations thereof, or other lightweight additives known in the art.


Gas-generating additives may be included in embodiments of the settable compositions to release gas at a predetermined time, which may be beneficial to prevent gas migration from the formation through the settable composition before it hardens. The generated gas may combine with or inhibit the permeation of the settable composition by formation gas. Examples of suitable gas-generating additives include, but are not limited to, metal particles (e.g., aluminum powder) that react with an alkaline solution to generate a gas.


Mechanical-property-enhancing additives may be included in embodiments of the settable compositions to, for example, ensure adequate compressive strength and long-term structural integrity. These properties can be affected by the strains, stresses, temperature, pressure, and impact effects from a subterranean environment. Examples of mechanical-property-enhancing additives include, but are not limited to, carbon fibers, glass fibers, metal fibers, mineral fibers, silica fibers, polymeric elastomers, and latexes.


Lost-circulation materials may be included in embodiments of the settable compositions to, for example, help prevent the loss of fluid circulation into the subterranean formation. Examples of lost-circulation materials include but are not limited to, cedar bark, shredded cane stalks, mineral fiber, mica flakes, cellophane, calcium carbonate, ground rubber, polymeric materials, pieces of plastic, grounded marble, wood, nut hulls, formica, corncobs, and cotton hulls.


Fluid-loss-control additives may be included in embodiments of the settable compositions to, for example, decrease the volume of fluid that is lost to the subterranean formation. Properties of the settable compositions may be significantly influenced by their water content. The loss of fluid can subject the settable compositions to degradation or complete failure of design properties. Examples of suitable fluid-loss-control additives include, but not limited to, certain polymers, such as hydroxyethyl cellulose, carboxymethylhydroxyethyl cellulose, copolymers of 2-acrylamido-2-methylpropanesulfonic acid and acrylamide or N,N-dimethylacrylamide, and graft copolymers comprising a backbone of lignin or lignite and pendant groups comprising at least one member selected from the group consisting of 2-acrylamido-2-methylpropanesulfonic acid, acrylonitrile, and N,N-dimethylacrylamide.


Foaming agents may be included in embodiments of the settable compositions to, for example, facilitate foaming and/or stabilize the resultant foam fowled therewith. Examples of suitable foaming additives 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 foaming additive is ZoneSealant™ 2000 agent, available from Halliburton Energy Services, Inc.


Defoaming additives may be included in embodiments of the settable compositions to, for example, reduce tendency for the settable composition to foam during mixing and pumping of the settable compositions. Examples of suitable defoaming additives include, but are not limited to, polyol silicone compounds. Suitable defoaming additives are available from Halliburton Energy Services, Inc., under the product name D-AIR™ defoamers.


Thixotropic additives may be included in embodiments of the settable compositions to, for example, provide a settable composition that can be pumpable as a thin or low viscosity fluid, but when allowed to remain quiescent attains a relatively high viscosity. Among other things, thixotropic additives may be used to help control free water, create rapid gelation as the slurry sets, combat lost circulation, prevent “fallback” in annular column, and minimize gas migration. Examples of suitable thixotropic additives include, but are not limited to, gypsum, water soluble carboxyalkyl, hydroxyalkyl, mixed carboxyalkyl hydroxyalkyl either of cellulose, polyvalent metal salts, zirconium oxychloride with hydroxyethyl cellulose, or a combination thereof.


Those of ordinary skill in the art will appreciate that the settable compositions generally should have a density suitable for a particular application. By way of example, the settable composition may have a density of about 4 pounds per gallon (“lb/gal”) to about 20 lb/gal. In certain embodiments, the settable compositions may have a density of from about 8 lb/gal to about 17 lb/gal. Embodiments of the settable 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. In some embodiments, the settable compositions may be foamed with one or more foaming additives and a gas. Those of ordinary skill in the art, with the benefit of this disclosure, should recognize the appropriate density for a particular application.


The components of the settable composition may be combined in any order desired to form a settable composition that can be placed into a subterranean formation. In addition, the components of the settable compositions may be combined using any mixing device compatible with the composition, including a bulk mixer, recirculating tub, or jet mixer, for example. In some embodiments, the settable compositions may be prepared by combining the dry components with water. Other additives may be combined with the water before it is added to the dry components. In some embodiments, the solid components may be dry blended prior to their combination with the water. For example, a dry blend may be prepared that comprises the wollastonite, kiln dust, and optional additive, such as the Portland cement, among others. Other suitable techniques may be used for preparation of the settable compositions as will be appreciated by those of ordinary skill in the art in accordance with certain embodiments.


In some embodiments, the settable compositions may develop a desirable compressive strength in the well bore annulus for subterranean cementing operations. Compressive strength is generally the capacity of a material or structure to withstand axially directed pushing forces. The compressive strength may be measured at a specified time after the settable composition has been positioned and the settable composition is maintained under specified temperature and pressure conditions. Compressive strength can be measured by either a destructive method or non-destructive method. The destructive method physically tests the strength of set compositions at various points in time by crushing the samples in a compression-testing machine. The compressive strength is calculated from the failure load divided by the cross-sectional area resisting the load and is reported in units of pound-force per square inch (psi). Non-destructive methods typically may employ an Ultrasonic Cement Analyzer (“UCA”), available from Fann Instrument Company, Houston, Tex. Compressive strengths may be determined in accordance with API RP 10B-2, Recommended Practice for Testing Well Cements, First Edition, July 2005.


By way of example, embodiments of the settable compositions may develop a 72-hour compressive strength in the subterranean formation in a range of from about 250 psi to about 10,000 psi and, alternatively, from about 800 psi about 2,000 psi. In some embodiments, the 72-hour compressive strength may be characterized as the destructive compressive strength as measured at atmospheric pressure and temperatures in a range of from about 50° F. to about 400° F., alternatively, in a range of from about 80° F. to about 250° F.


Embodiments of the settable compositions may be used in a variety of applications, including subterranean cementing applications such as primary and remedial cementing, among others. Embodiments may include providing a settable composition and allowing the settable composition to set. Embodiments of the settable compositions may comprise wollastonite, kiln dust, and water. Additional additives may be included in the settable compositions, as described above, for example. As used herein, introducing the settable composition into a subterranean formation includes introduction into any portion of the subterranean formation, including, without limitation, into a well bore drilled into the subterranean formation, into a near well bore region surrounding the well bore, or into both. Moreover, introducing the settable composition into the subterranean formation is intended to encompass introduction of the settable composition into one or more subterranean formations that are penetrated by the well bore.


In primary-cementing embodiments, for example, a settable composition may be introduced into a well-bore annulus and allowed to set in the well-bore annulus to form a hardened mass. The well-bore annulus may include, for example, an annular space between a conduit (e.g., pipe string, surface casing, intermediate casing, production casing, liner, etc.) and a wall of a well bore or between the conduit and a larger conduit in the well bore. Generally, in most instances, the hardened mass should fix the conduit in the well bore.


In remedial-cementing embodiments, a settable composition may be used, for example, in squeeze-cementing operations or in the placement of plugs. By way of example, the settable composition may be placed in a well bore to plug a void or crack in the formation, in a gravel pack, in the conduit, in the cement sheath, and/or a microannulus between the cement sheath and the conduit. In another embodiment, the settable composition may be placed into a well bore to form a plug in the well bore with the plug, for example, sealing the well bore.


Referring now to FIG. 1, preparation a settable composition in accordance with example embodiments will now be described. FIG. 1 illustrates a system 2 for preparation of a settable composition and delivery to a well bore in accordance with certain embodiments. As shown, the settable composition may be mixed in mixing equipment 4, such as a jet mixer, re-circulating mixer, or a batch mixer, for example, and then pumped via pumping equipment 6 to the well bore. In some embodiments, the mixing equipment 4 and the pumping equipment 6 may be disposed on one or more cement trucks as will be apparent to those of ordinary skill in the art. In some embodiments, a jet mixer may be used, for example, to continuously mix the wollastonite/pumice with the water as it is being pumped to the well bore.


An example technique for placing a settable composition into a subterranean formation will now be described with reference to FIGS. 2A and 2B. FIG. 2A illustrates surface equipment 10 that may be used in placement of a settable composition in accordance with certain embodiments. It should be noted that while FIG. 2A generally depicts a land-based operation, those skilled in the art will readily recognize that the principles described herein are equally applicable to subsea operations that employ floating or sea-based platforms and rigs, without departing from the scope of the disclosure. As illustrated by FIG. 2A, the surface equipment 10 may include a cementing unit 12, which may include one or more cement trucks. The cementing unit 12 may include mixing equipment 4 and pumping equipment 6 (e.g., FIG. 1) as will be apparent to those of ordinary skill in the art. The cementing unit 12 may pump a settable composition 14 through a feed pipe 16 and to a cementing head 18 which conveys the settable composition 14 downhole.


Turning now to FIG. 2B, the settable composition 14 may be placed into a subterranean formation 20 in accordance with example embodiments. As illustrated, a well bore 22 may be drilled into the subterranean formation 20. While well bore 22 is shown extending generally vertically into the subterranean formation 20, the principles described herein are also applicable to well bores that extend at an angle through the subterranean formation 20, such as horizontal and slanted well bores. As illustrated, the well bore 22 comprises walls 24. In the illustrated embodiment, a surface casing 26 has been inserted into the well bore 22. The surface casing 26 may be cemented to the walls 24 of the well bore 22 by cement sheath 28. In the illustrated embodiment, one or more additional conduits (e.g., intermediate casing, production casing, liners, etc.), shown here as casing 30 may also be disposed in the well bore 22. As illustrated, there is a well bore annulus 32 formed between the casing 30 and the walls 24 of the well bore 22 and/or the surface casing 26. One or more centralizers 34 may be attached to the casing 30, for example, to centralize the casing 30 in the well bore 22 prior to and during the cementing operation.


With continued reference to FIG. 2B, the settable composition 14 may be pumped down the interior of the casing 30. The settable composition 14 may be allowed to flow down the interior of the casing 30 through the casing shoe 42 at the bottom of the casing 30 and up around the casing 30 into the well bore annulus 32. The settable composition 14 may be allowed to set in the well bore annulus 32, for example, to form a cement sheath that supports and positions the casing 30 in the well bore 22. While not illustrated, other techniques may also be utilized for introduction of the settable composition 14. By way of example, reverse circulation techniques may be used that include introducing the settable composition 14 into the subterranean formation 20 by way of the well bore annulus 32 instead of through the casing 30.


As it is introduced, the settable composition 14 may displace other fluids 36, such as drilling fluids and/or spacer fluids, that may be present in the interior of the casing 30 and/or the well bore annulus 32. At least a portion of the displaced fluids 36 may exit the well bore annulus 32 via a flow line 38 and be deposited, for example, in one or more retention pits 40 (e.g., a mud pit), as shown on FIG. 2A. Referring again to FIG. 2B, a bottom plug 44 may be introduced into the well bore 22 ahead of the settable composition 14, for example, to separate the settable composition 14 from the fluids 36 that may be inside the casing 30 prior to cementing. After the bottom plug 44 reaches the landing collar 46, a diaphragm or other suitable device rupture to allow the settable composition 14 through the bottom plug 44. In FIG. 2B, the bottom plug 44 is shown on the landing collar 46. In the illustrated embodiment, a top plug 48 may be introduced into the well bore 22 behind the settable composition 14. The top plug 48 may separate the settable composition 14 from a displacement fluid 50 and also push the settable composition 14 through the bottom plug 44.


The exemplary settable compositions disclosed herein may directly or indirectly affect one or more components or pieces of equipment associated with the preparation, delivery, recapture, recycling, reuse, and/or disposal of the disclosed settable compositions. For example, the disclosed settable compositions may directly or indirectly affect one or more mixers, related mixing equipment, mud pits, storage facilities or units, composition separators, heat exchangers, sensors, gauges, pumps, compressors, and the like used generate, store, monitor, regulate, and/or recondition the exemplary settable compositions. The disclosed settable compositions may also directly or indirectly affect any transport or delivery equipment used to convey the settable compositions to a well site or downhole such as, for example, any transport vessels, conduits, pipelines, trucks, tubulars, and/or pipes used to compositionally move the settable compositions from one location to another, any pumps, compressors, or motors (e.g., topside or downhole) used to drive the settable compositions into motion, any valves or related joints used to regulate the pressure or flow rate of the settable compositions, and any sensors (i.e., pressure and temperature), gauges, and/or combinations thereof, and the like. The disclosed settable compositions may also directly or indirectly affect the various downhole equipment and tools that may come into contact with the settable compositions such as, but not limited to, wellbore casing, wellbore liner, completion string, insert strings, drill string, coiled tubing, slickline, wireline, drill pipe, drill collars, mud motors, downhole motors and/or pumps, cement pumps, surface-mounted motors and/or pumps, centralizers, turbolizers, scratchers, floats (e.g., shoes, collars, valves, etc.), logging tools and related telemetry equipment, actuators (e.g., electromechanical devices, hydromechanical devices, etc.), sliding sleeves, production sleeves, plugs, screens, filters, flow control devices (e.g., inflow control devices, autonomous inflow control devices, outflow control devices, etc.), couplings (e.g., electro-hydraulic wet connect, dry connect, inductive coupler, etc.), control lines (e.g., electrical, fiber optic, hydraulic, etc.), surveillance lines, drill bits and reamers, sensors or distributed sensors, downhole heat exchangers, valves and corresponding actuation devices, tool seals, packers, cement plugs, bridge plugs, and other wellbore isolation devices, or components, and the like.


EXAMPLES

To facilitate a better understanding of the present invention, the following examples of some of the preferred embodiments are given. In no way should such examples be read to limit, or to define, the scope of the invention.


Example 1

The following series of tests was performed to evaluate the force resistance properties of settable compositions comprising wollastonite, cement kiln dust, and Portland cement. Three different sample settable compositions, designated Samples 1 to 3, were prepared that comprised cement kiln dust, wollastonite, Portland Class H cement and sufficient water to provide the density indicated in the table below. The samples were prepared by combining these solid components with water while mixing in a Waring blender. The concentrations of the wollastonite, cement kiln dust, and Portland Class H cement were varied as indicated in the table below. The wollastonite was supplied Seaforth Mineral & Ore Co., East Liverpool, Ohio. The cement kiln dust was supplied Holcem Cement Company, Ada, Okla.


After preparation, the samples were allowed to cure for seventy-two hours in 2″ by 4″ metal cylinders that were placed in a water bath at 170° F. to form set cylinders and the resulting set cylinders were tested for mechanical properties in accordance with API RP 10B-2. The mixability was also observed and recorded. A slurry that was thick indicates that there was insufficient water. A slurry that was mixable indicates proper weight and proper amount of water.


The results of the tests are set forth in the table below. The data reported in the table below is the average of 3 tests for each of sample. The abbreviation “% bwoc” indicates the weight percent of the particular component by weight of the cementitious components, which were the cement kiln dust, the wollastonite, and the Portland Class H Cement. The abbreviation “gal/sk” indicates the weight of the particular component per 94 pound sack of cementitious components. The abbreviation “psi” refers to pounds per square inch.









TABLE 1







Compressive Strength Tests
















72-Hr







Compressive



Density
Cementitious Components
Water
Strength













Sample No.
(lb/gal)
Material
% bwoc
(gal/sk)
(psi)
Mixability
















1
14.2
Cement Kiln Dust
25
7.0261
876
Slurry




Wollastonite
25


Mixable




Class H Cement
50


2
14.5
Cement Kiln Dust
25
6.5039
1136
Slurry




Wollastonite
25


Thick




Class H Cement
50


3
14.5
Cement Kiln Dust
50
6.1521
611
Slurry




Wollastonite
25


Mixable




Class H Cement
25









Example 2

An additional test was performed to evaluate the force resistance properties of foamed settable compositions comprising wollastonite, cement kiln dust, and Portland cement. A base sample composition was prepared that comprised cement kiln dust, wollastonite, Portland Class H cement and sufficient water to have a density of 14.2 lb/gal. The base sample was prepared by combining the solid components with water while mixing in a Waring blender. The wollastonite was supplied Seaforth Mineral & Ore Co., East Liverpool, Ohio. The cement kiln dust was supplied Holcem Cement Company, Ada, Okla. A foaming agent (ZoneSealant™ 2000 agent, Halliburton Energy Services, Inc.) was then added to the base sample composition in an amount of 2% bwoc. Next, the base composition was foamed down to 12.5 lb/gal by mixing in a Waring blender.


After preparation, the sample was allowed to cure for seventy-two hours in 2″ by 4″ metal cylinders that were placed in a water bath at 170° F. to form set cylinders and the resulting set cylinders were tested for mechanical properties in accordance with API RP 10B-2. The result is set forth in the table below. The data reported in the table below is the average of 3 tests for the sample. The abbreviation “% bwoc” indicates the weight percent of the particular component by weight of the cement components, which were the cement kiln dust, the wollastonite, and the Portland Class H Cement.









TABLE 2







Compressive Strength Tests















72- Hr





Foaming
Compressive


Sample
Density
Cementitious Components
Agent
Strength












No.
(lb/gal)
Material
% bwoc
(% bwoc)
(psi)





4
12.5
Cement Kiln Dust
25
2
190.3




Wollastonite
25




Class H Cement
50









Example 3

An additional test was performed to evaluate the force resistance properties of a settable composition comprising wollastonite, cement kiln dust, and hydrated lime. A sample settable composition was prepared that comprised cement kiln dust, wollastonite, hydrated lime, a dispersant, and sufficient water to provide the density indicated in the table below. The sample was prepared by combining the solid components with water while mixing in a Waring blender. The wollastonite was supplied Seaforth Mineral & Ore Co., East Liverpool, Ohio. The cement kiln dust was supplied Holcem Cement Company, Ada, Okla. The dispersant is available from Halliburton Energy Services, Inc., as CFR-3™ dispersant.


After preparation, the sample was allowed to cure for seventy-two hours in 2″ by 4″ metal cylinders that were placed in a water bath at 170° F. to form set cylinders and the resulting set cylinders were tested for mechanical properties in accordance with API RP 10B-2. The result is set forth in the table below. The data reported in the table below is the average of 3 tests of the sample. The abbreviation “% bwoc” indicates the weight percent of the particular component by weight of the cement components, which were the cement kiln dust, wollastonite, and hydrated lime.









TABLE 3







Compressive Strength Tests












Cementitious

72-Hr




Components

Compressive














Sample
Density

%
Dispersant
Water
Strength



No.
(lb/gal)
Material
bwoc
(% bwoc)
(gal/sk)
(psi)
Mixability

















5
14.2
Cement Kiln Dust
45.5
0.6
7.0454
207
Slurry Mixable After




Wollastonite
45.5



Adding Dispersant




Hydrated Lime
9









Example 4

The following series of tests was performed to evaluate the force resistance properties of settable compositions comprising wollastonite, cement kiln dust, and Portland cement, and optional additives. Five different sample settable compositions, designated Samples 6 to 10, were prepared that comprised cement kiln dust, wollastonite, Portland Class H cement, one or more optional additives and sufficient water to provide the density indicated in the table below. The samples were prepared by combining the solid components with water while mixing in a Waring blender. A dispersant (CFR-3™ dispersant) was also included in Samples 6 and 10. The concentrations of the wollastonite, cement kiln dust, Portland Class H cement, and optional additive(s) were varied as indicated in the table below. The wollastonite was supplied Seaforth Mineral & Ore Co., East Liverpool, Ohio. The cement kiln dust was supplied Holcem Cement Company, Ada, Okla.


The optional additives included in the samples were metakaolin, fly ash, silica flour, vitrified shale, and fumed silica. Sample 6 included metakaolin supplied by BASF Corporation, Floraham Park, N.J. Sample 7 included fly ash supplied by Fairfield Poz, Fairfield, Tex. Samples 8 included silica flour available from Halliburton Energy Services, as SSA-1™ strength-stabilizing agent. Sample 9 included shale available from TXI, Midloathian, Tex. Sample 10 included fumed silica available from Halliburton Energy Services, Inc., as Silicalite™ cement additive


After preparation, the samples were allowed to cure for seventy-two hours in 2″ by 4″ metal cylinders that were placed in a water bath at 170° F. to foam set cylinders and the resulting set cylinders were tested for mechanical properties in accordance with API RP 10B-2. The results of the tests are set forth in the table below. The data reported in the table below is the average of 3 tests for each of the samples. The abbreviation “% bwoc” indicates the weight percent of the particular component by weight of the listed cementitious components.









TABLE 4







Compressive Strength Tests












Cementitious

72-Hr




Components

Compressive














Sample
Density

%
Dispersant
Water
Strength



No.
(lb/gal)
Material
bwoc
(% bwoc)
(gal/sk)
(psi)
Mixability

















6
14.5
Cement Kiln Dust
25
0.6
6.1521
2060
Slurry Mixable




Wollastonite
25




Class H Cement
25




Metakaolin
25


7
14.5
Cement Kiln Dust
25

5.8950
1965
Slurry Mixable




Wollastonite
25




Class H Cement
25




Fly Ash
25


8
14.5
Cement Kiln Dust
25

6.0688
548
Slurry Mixable




Wollastonite
25




Class H Cement
25




Silica Flour
25


9
14.5
Cement Kiln Dust
25

5.9899
1415
Slurry Mixable




Wollastonite
25




Class H Cement
25




Shale
25


10
14.5
Cement Kiln Dust
25
1  
6.4124
1108
Difficult to mix




Wollastonite
25



and pour into




Class H Cement
25



cylinders




Fumed Silica
25









It should be understood that the compositions and methods are described in terms of “comprising,” “containing,” or “including” various components or steps, the compositions and methods can also “consist essentially of” or “consist of” the various components and steps. Moreover, the indefinite articles “a” or “an,” as used in the claims, are defined herein to mean one or more than one of the element that it introduces.


For the sake of brevity, only certain ranges are explicitly disclosed herein. However, ranges from any lower limit may be combined with any upper limit to recite a range not explicitly recited, as well as, ranges from any lower limit may be combined with any other lower limit to recite a range not explicitly recited, in the same way, ranges from any upper limit may be combined with any other upper limit to recite a range not explicitly recited. Additionally, whenever a numerical range with a lower limit and an upper limit is disclosed, any number and any included range falling within the range is specifically disclosed. 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 to set forth every number and range encompassed within the broader range of values even if not explicitly recite. Thus, every point or individual value may serve as its own lower or upper limit combined with any other point or individual value or any other lower or upper limit, to recite a range not explicitly recited.


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. Although individual embodiments are discussed, the invention covers all combinations of all those embodiments. Furthermore, no limitations are intended to the details of construction or design herein shown, other than as described in the claims below. Also, the teens in the claims have their plain, ordinary meaning unless otherwise explicitly and clearly defined by the patentee. 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. If there is any conflict in the usages of a word or tem in this specification and one or more patent(s) or other documents that may be incorporated herein by reference, the definitions that are consistent with this specification should be adopted.

Claims
  • 1. A cementing system comprising: kiln dust;wollastonite in an amount of from 10% to about 75% by weight of the total amount of cementitious components in the cementing system, wherein the kiln dust is present in an amount in a range of from about 5% to about 90% by weight of the total amount of cementitious components present in the cementing system; andwater present in an amount sufficient to from a pumpable slurry.
  • 2. The cementing system of claim 1 wherein the kiln dust comprises at least one partially calcined kiln feed selected from the group consisting of cement kiln dust, lime kiln dust, and a combination thereof.
  • 3. The cementing system of claim 1 wherein the kiln dust comprises SiO2, Al2O3, Fe2O3, CaO, MgO, SO3, Na2O, and K2O.
  • 4. The cementing system of claim 1 wherein the kiln dust is present in the settable composition in an amount in a range of from about 5% to about 50% by weight of the total amount of cementitious components present in the cementing system.
  • 5. The cementing system of claim 1 wherein the wollastonite is present in the settable composition in an amount in a range of from about 20% to about 75% by weight of the total amount of cementitious components present in the cementing system.
  • 6. The cementing system of claim 1 wherein the cementing system further comprises Portland cement.
  • 7. The cementing system of claim 6 wherein the Portland cement is present in the cementing system in an amount in a range of from about 1% to about 75% by weight of the total amount of cementitious components present in the cementing system.
  • 8. The cementing system of claim 6 wherein the Portland cement is present in the cementing system in an amount in a range of from about 10% to about 50% by weight of the total amount of cementitious components present in the cementing system, wherein the kiln dust is present in the cementing system in an amount in a range of from about 10% to about 50% by weight of the total amount of cementitious components present in the cementing system, and wherein the wollastonite is present in the cementing system in an amount in a range of from about 10% to about 50% by weight of the total amount of cementitious components present in the cementing system.
  • 9. The cementing system of claim 1 further comprising at least one additive selected from the group consisting of fly ash, slag, shale, zeolite, metakaolin, pumice, perlite, lime, silica, rice husk ash, small-particle size cement, and any combination thereof.
  • 10. The cementing system of claim 1 further comprising at least one additive selected from the group consisting of a dispersant, a strength-retrogression additive, a set accelerator, a set retarder, a weighting agent, a lightweight additive, a gas-generating additive, a mechanical property enhancing additive, a lost-circulation material, a fluid loss control additive, a foaming additive, a defoaming additive, an oil-swellable particle, a water-swellable particle, a thixotropic additive, crystalline silica, fumed silica, silicates, salts, fibers, hydratable clays, microspheres, diatomaceous earth, elastomers, elastomeric particles, resins, latex and any combination thereof.
  • 11. The cementing system of claim 1 further comprising: a foaming agent; anda gas.
  • 12. The cementing system of claim 1 further comprising: mixing equipment for mixing the cementing system; andpumping equipment for delivering the cementing system into a well bore.
  • 13. A cement composition comprising: cement kiln dust;wollastonite in a amount of from 10% to about 75% by weight of the total amount of cementitious components in the cementing system, wherein the kiln dust is present in an amount in a range of from about 5% to about 90% by weight of the total amount of cementitious components present in the cementing system;hydraulic cement; andwater present in amount sufficient to from a pumpable slurry.
  • 14. The cement composition of claim 13 further comprising an additive selected from the group consisting of fly ash, slag, shale, zeolite, metakaolin, pumice, perlite, lime, silica, rice husk ash, small-particle size cement, and any combination thereof.
  • 15. The cement composition of claim 13 wherein the cement kiln dust is present in the cement composition in an amount in a range of from about 5% to about 90% by weight of the total amount of cementitious components present in the cement composition, wherein the wollastonite is present in the cement composition in an amount in a range of from about 10% to about 50% by weight of the total amount of cementitious components present in the cement composition, and wherein the hydraulic cement is present in an amount in a range of from about 1% to about 75% by weight of the total amount of cementitious components present in the cement composition.
  • 16. The cement composition of claim 13 wherein the cement composition further comprises metakaolin in an amount in a range of from about 10% to about 50% by weight of the total amount of cementitious components present in the cement composition.
  • 17. The cement composition of claim 13 further comprising: a foaming agent; anda gas.
  • 18. A cement composition comprising: cement kiln dust in an amount in a range of from about 5% to about 90% by weight of the total amount of cementitious components present in the cement composition;wollastonite present in an amount in a range of from about 10% to about 75% by weight of the total amount of cementitious components present in the cement composition;Portland cement present in an amount in a range of from about 1% to about 75% by weight of a total amount of cementitious components present in the cement composition;water present in an amount sufficient to form a pumpable slurry; andoptionally, an additive selected from the group consisting of fly ash, slag, shale, zeolite, metakaolin, pumice, perlite, lime, silica, rice husk ash, small-particle size cement, a foaming agent, a gas, and any combination thereof.
CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a divisional of U.S. patent application Ser. No. 13/955,516, filed Jul. 31, 2013, which is a continuation-in-part of U.S. patent application Ser. No. 13/477,777, filed on May 22, 2012, which is a divisional of U.S. patent application Ser. No. 13/399,913, filed on Feb. 17, 2012 (now issued as U.S. Pat. No. 8,281,859), which is a continuation-in-part of U.S. patent application Ser. No. 13/180,238, filed on Jul. 11, 2011, which is a continuation-in-part of U.S. patent application Ser. No. 12/975,196, filed on Dec. 21, 2010 (now issued as U.S. Pat. No. 8,403,045), and U.S. patent application Ser. No. 13/399,913 is also a continuation-in-part of U.S. patent application Ser. No. 12/895,436, filed on Sep. 30, 2010 (now issued as U.S. Pat. No. 8,522,873), which is a continuation-in-part of U.S. patent application Ser. No. 12/264,010, filed on Nov. 3, 2008 (now issued as U.S. Pat. No. 8,333,240), which is a continuation-in-part of U.S. patent application Ser. No. 11/223,669, filed Sep. 9, 2005 (now issued as U.S. Pat. No. 7,445,669), the entire disclosures of which are incorporated herein by reference.

US Referenced Citations (434)
Number Name Date Kind
1931921 Breerwood Oct 1933 A
2021956 Gladney et al. Nov 1935 A
2045899 Davis Jun 1936 A
2094316 Cross et al. Sep 1937 A
2133622 Larmour et al. Oct 1938 A
2144254 Breerwood Jan 1939 A
2193775 Stratford Mar 1940 A
2193807 Dieterich Mar 1940 A
2214715 Breerwood Sep 1940 A
2329940 Ponzer Sep 1943 A
2592468 Rex et al. Apr 1952 A
2772739 Aire Dec 1956 A
2842205 Allen et al. Jul 1958 A
2844361 Dilcher et al. Jul 1958 A
2848051 Willaims Aug 1958 A
2871133 Palonen et al. Jan 1959 A
2880096 Hurley Mar 1959 A
2945769 Gama et al. Jul 1960 A
3024125 Lee Mar 1962 A
3066031 Schifferle Nov 1962 A
3168139 Kennedy et al. Feb 1965 A
3320077 Prior May 1967 A
3411580 Roberts et al. Nov 1968 A
3421703 Galer Jan 1969 A
3454095 Messenger et al. Jul 1969 A
3467193 Messenger Sep 1969 A
3473939 Mayberry et al. Oct 1969 A
3499491 Wyant et al. Mar 1970 A
3557876 Tragesser Jan 1971 A
3574113 Shannom Apr 1971 A
3574816 Abbdellatif et al. Apr 1971 A
3628973 Greening et al. Dec 1971 A
3748159 George Jul 1973 A
3749173 Hill et al. Jul 1973 A
3863718 Bruist Feb 1975 A
3876005 Fincher et al. Apr 1975 A
3887009 Miller et al. Jun 1975 A
3887385 Quist et al. Jun 1975 A
3921717 Danjushevsky et al. Nov 1975 A
3959007 Pitt May 1976 A
4018617 Nicholson Apr 1977 A
4018619 Webster et al. Apr 1977 A
4031184 McCord Jun 1977 A
4036301 Powers et al. Jul 1977 A
4083407 Griffin et al. Apr 1978 A
4101332 Nicholson Jul 1978 A
4105459 Mehta Aug 1978 A
4141843 Watson Feb 1979 A
4160674 Sawyer Jul 1979 A
4176720 Wilson Dec 1979 A
4268316 Wills et al. May 1981 A
4274881 Langton et al. Jun 1981 A
4304300 Watson Dec 1981 A
4333764 Richardson Jun 1982 A
4341562 Ahlbeck Jul 1982 A
RE31190 Detroit et al. Mar 1983 E
4400474 Copperthwaite et al. Aug 1983 A
4407677 Wills et al. Oct 1983 A
4423781 Thomas Jan 1984 A
4432800 Kneller et al. Feb 1984 A
4435216 Diehl et al. Mar 1984 A
4436850 Burdick et al. Mar 1984 A
4440576 Flannery et al. Apr 1984 A
4460292 Durham et al. Jul 1984 A
4462835 Car Jul 1984 A
4470463 Holland Sep 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
4633950 Delhommer et al. Jan 1987 A
4676317 Fry et al. Jun 1987 A
4676832 Childs et al. Jun 1987 A
4741782 Styron May 1988 A
4761183 Clarke Aug 1988 A
4784223 Worrall et al. Nov 1988 A
4829107 Kindt May 1989 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
5113943 Wilson et al. May 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
5183505 Spinney Feb 1993 A
5183506 Zhang Feb 1993 A
5213160 Nahm et al. May 1993 A
5215585 Luthra et al. Jun 1993 A
5238064 Dahl et al. Aug 1993 A
5252128 Gopalkrishnan Oct 1993 A
5266111 Barbour Nov 1993 A
5290355 Jakel et al. Mar 1994 A
5295543 Terry et al. Mar 1994 A
5305831 Nahm Apr 1994 A
5314022 Cowan et al. May 1994 A
5316083 Nahm et al. May 1994 A
5327968 Onan et al. Jul 1994 A
5337824 Cowan Aug 1994 A
5339902 Harris Aug 1994 A
5346012 Heathman Sep 1994 A
5346548 Mehta 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
5417759 Huddleston May 1995 A
5421409 Mueller et al. Jun 1995 A
5423379 Hale et al. Jun 1995 A
5430235 Hooykaas et al. Jul 1995 A
5439056 Cowan Aug 1995 A
5456751 Zandi et al. Oct 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
5478391 Babaev 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
5529123 Carpenter et al. Jun 1996 A
5529624 Riegler Jun 1996 A
5536311 Rodrigues Jul 1996 A
5542782 Carter et al. Aug 1996 A
5554352 Jaques et al. Sep 1996 A
5569324 Totten et al. Oct 1996 A
5571318 Griffith Nov 1996 A
5580379 Cowan Dec 1996 A
5584926 Borgholm et al. Dec 1996 A
5585333 Dahl et al. Dec 1996 A
5588489 Chatterji et al. Dec 1996 A
5626665 Barger et al. May 1997 A
5641584 Andersen et al. Jun 1997 A
5673753 Hale et al. Oct 1997 A
5681384 Liskowitz Oct 1997 A
5688844 Chatterji et al. Nov 1997 A
5711383 Terry et al. Jan 1998 A
5716910 Totten et al. Feb 1998 A
5728654 Dobson et al. Mar 1998 A
5788762 Barger et al. Aug 1998 A
5795924 Chatterji et al. Aug 1998 A
5820670 Chatterji et al. Oct 1998 A
5851960 Totten et al. Dec 1998 A
5866516 Costin Feb 1999 A
5866517 Carpenter et al. 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
6098711 Chatterji et al. Aug 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
6264738 Lorke 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
6328106 Griffith et al. Dec 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
6416574 Steelhammer et al. Jul 2002 B1
6451104 Mehta Sep 2002 B2
6457524 Roddy et al. Oct 2002 B1
6478869 Reddy et al. Nov 2002 B2
6478870 Marko Nov 2002 B2
6488763 Brothers et al. Dec 2002 B2
6488764 Westerman Dec 2002 B2
6494951 Reddy et al. Dec 2002 B1
6500252 Chatterji et al. Dec 2002 B1
6502634 Evans et al. Jan 2003 B1
6508305 Brannon et al. Jan 2003 B1
6516884 Chatterji et al. Feb 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
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
6641658 Dubey Nov 2003 B1
6645289 Sobolev et al. Nov 2003 B2
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
6668927 Chatterji et al. Dec 2003 B1
6668929 Griffith et al. Dec 2003 B2
6689208 Brothers Feb 2004 B1
6702044 Reddy et al. Mar 2004 B2
6706108 Polston Mar 2004 B2
6708760 Chatterji et al. Mar 2004 B1
6715568 Bailey Apr 2004 B1
6716282 Griffith et al. Apr 2004 B2
6729405 DiLullo et al. May 2004 B2
6749679 Shi Jun 2004 B2
6755905 Oates Jun 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
6832652 Dillenbeck et al. Dec 2004 B1
6835243 Brothers et al. Dec 2004 B2
6837316 Reddy et al. Jan 2005 B2
6840318 Lee Jan 2005 B2
6840996 Morioka et al. Jan 2005 B2
6846357 Reddy et al. Jan 2005 B2
6848519 Reddy et al. Feb 2005 B2
6869474 Perez-Pena et al. Mar 2005 B2
6869475 Krowl Mar 2005 B1
6874578 Garnier Apr 2005 B1
6883609 Drochon Apr 2005 B2
6887833 Brothers et al. May 2005 B2
6889767 Reddy et al. May 2005 B2
6899177 Chatterj et al. May 2005 B2
6904971 Brothers et al. Jun 2005 B2
6908507 Lalande et al. Jun 2005 B2
6908508 Brothers Jun 2005 B2
6911078 Barlet-Gouedard et al. Jun 2005 B2
6964302 Luke et al. Nov 2005 B2
6989057 Getzlaf et al. Jan 2006 B2
7022755 Chatterji et al. Apr 2006 B1
7048053 Santra et al. May 2006 B2
7055603 Caveny et al. Jun 2006 B2
7073584 Reddy et al. Jul 2006 B2
7073585 Morgan et al. Jul 2006 B2
7077203 Roddy et al. Jul 2006 B1
7096944 Vargo et al. Aug 2006 B2
7101829 Guichard Sep 2006 B2
7137446 Gagliano et al. Nov 2006 B2
7140439 Luke et al. Nov 2006 B2
7140440 Luke et al. Nov 2006 B2
7143827 Chatterji et al. Dec 2006 B2
7147055 Brothers et al. Dec 2006 B2
7147067 Getzlaf et al. Dec 2006 B2
7150321 Luke et al. Dec 2006 B2
7156173 Mueller Jan 2007 B2
7156174 Roddy Jan 2007 B2
7174962 Roddy et al. Feb 2007 B1
7178597 Reddy Feb 2007 B2
7182137 Fyten et al. Feb 2007 B2
7198104 Griffith et al. Apr 2007 B2
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
7217441 Bour et al. May 2007 B2
7219733 Luke et al. May 2007 B2
7255739 Brothers et al. Aug 2007 B2
7284609 Roddy et al. Oct 2007 B2
7284611 Reddy Oct 2007 B2
7284930 Shi et al. Oct 2007 B2
7285164 Luke et al. Oct 2007 B2
7293609 Dealy et al. Nov 2007 B2
7297664 Santra et al. Nov 2007 B2
7303008 Badalamenti et al. Dec 2007 B2
7303015 Fyten et al. Dec 2007 B2
7316744 De La Roij et al. Jan 2008 B2
7325611 Santra et al. Feb 2008 B2
7326291 Fyten Feb 2008 B2
7332026 Fyten Feb 2008 B2
7335252 Roddy et al. Feb 2008 B2
7337842 Roddy et al. Mar 2008 B2
7338923 Roddy et al. Mar 2008 B2
7341104 Roddy et al. Mar 2008 B2
7341105 Bingamon et al. Mar 2008 B2
7350573 Reddy Apr 2008 B2
7353870 Roddy et al. Apr 2008 B2
7381263 Roddy et al. Jun 2008 B2
7387675 Roddy et al. Jun 2008 B2
7395860 Roddy et al. Jul 2008 B2
7404855 Chatterji et al. Jul 2008 B2
7409990 Burts et al. Aug 2008 B1
7413014 Chatterji et al. Aug 2008 B2
7424914 Reddy Sep 2008 B2
7442249 Mueller Oct 2008 B2
7445669 Roddy et al. Nov 2008 B2
7478675 Roddy et al. Jan 2009 B2
7488705 Reddy Feb 2009 B2
7493968 Reddy Feb 2009 B2
7527688 Bingamon et al. May 2009 B2
7537054 Reddy May 2009 B2
7544640 Luke et al. Jun 2009 B2
7607482 Roddy et al. Oct 2009 B2
7607484 Roddy et al. Oct 2009 B2
7612021 Chatterji Nov 2009 B2
7627870 Michaeli et al. Dec 2009 B1
7631692 Roddy et al. Dec 2009 B2
7647970 Mueller Jan 2010 B2
7651563 Datta et al. Jan 2010 B2
7655088 Bethani Feb 2010 B2
7658796 Nordmeyer Feb 2010 B2
7674332 Roddy et al. Mar 2010 B2
7712527 Roddy May 2010 B2
7740070 Santra et al. Jun 2010 B2
7741841 Edwards et al. Jun 2010 B2
7743828 Roddy et al. Jun 2010 B2
7748454 Reddy et al. Jul 2010 B2
7762329 Morgan Jul 2010 B1
7784542 Roddy et al. Aug 2010 B2
7789150 Roddy et al. Sep 2010 B2
7815880 Constantz et al. Oct 2010 B2
7837412 O'Hearn Nov 2010 B2
7867954 Warrender et al. Jan 2011 B2
7887694 Constantz et al. Feb 2011 B2
7919064 Kawatra et al. Apr 2011 B2
7922809 Constantz et al. Apr 2011 B1
7927419 Roddy Apr 2011 B2
7939336 Constantz et al. May 2011 B2
7963323 Bailey et al. Jun 2011 B2
7993451 Brouillette et al. Aug 2011 B2
8006446 Constantz et al. Aug 2011 B2
8012582 Luo Sep 2011 B2
8029618 Al-Shafei Oct 2011 B2
8030253 Roddy et al. Oct 2011 B2
8039253 Asou et al. Oct 2011 B2
8062999 Reddy Nov 2011 B2
8123852 Reddy Feb 2012 B2
8143198 Lewis et al. Mar 2012 B2
8162055 Lewis et al. Apr 2012 B2
8183186 Luo May 2012 B2
8261827 Roddy Sep 2012 B2
8261833 Nguyen Sep 2012 B2
8281859 Roddy Oct 2012 B2
8297357 Brenneis Oct 2012 B2
8307899 Brenneis Nov 2012 B2
8318642 Roddy Nov 2012 B2
8324137 Roddy et al. Dec 2012 B2
8327939 Roddy Dec 2012 B2
8333240 Roddy Dec 2012 B2
8342242 Roddy et al. Jan 2013 B2
8383558 Reddy Feb 2013 B2
8394744 Woytowich et al. Mar 2013 B2
8399387 Roddy Mar 2013 B2
8403045 Brenneis et al. Mar 2013 B2
8434553 Brenneis May 2013 B2
8440596 Brenneis May 2013 B2
8470275 Constantz et al. Jun 2013 B2
8486868 Brenneis Jul 2013 B2
8486869 Brenneis et al. Jul 2013 B2
8505629 Benkley et al. Aug 2013 B2
8505630 Chatterji Aug 2013 B2
8522873 Benkley et al. Sep 2013 B2
8544543 Chatterji Oct 2013 B2
8551923 Benkley et al. Oct 2013 B1
8554543 Cherepanov et al. Oct 2013 B2
8555967 Chatterji et al. Oct 2013 B2
8557036 Chatterji et al. Oct 2013 B1
8672028 Karcher et al. Mar 2014 B2
8691737 Chatterji et al. Apr 2014 B2
20020117090 Ku Aug 2002 A1
20030116887 Scott Jun 2003 A1
20040187740 Timmons Sep 2004 A1
20040194960 DiLullo Oct 2004 A1
20040256102 Trato Dec 2004 A1
20050166803 Dillenbeck Aug 2005 A1
20060166834 Roddy Jul 2006 A1
20070056479 Gray Mar 2007 A1
20070137528 Le Roy-Delage et al. Jun 2007 A1
20080229979 Lewis Sep 2008 A1
20080300149 Reddy et al. Dec 2008 A1
20090124522 Roddy et al. May 2009 A1
20090169452 Constantz et al. Jul 2009 A1
20090202410 Kawatra et al. Aug 2009 A1
20100025039 Roddy et al. Feb 2010 A1
20100044057 Dealy et al. Feb 2010 A1
20100081584 Perez Apr 2010 A1
20100196104 Constantz et al. Aug 2010 A1
20100258035 Constantz et al. Oct 2010 A1
20100273912 Roddy et al. Oct 2010 A1
20100282466 Brenneis Nov 2010 A1
20100294496 Woytowich et al. Nov 2010 A1
20110000400 Roddy Jan 2011 A1
20110017452 Benkley et al. Jan 2011 A1
20110073311 Porcherie Mar 2011 A1
20110297378 Reddy et al. Dec 2011 A1
20120012315 Woytowich et al. Jan 2012 A1
20120145387 Pyatina et al. Jun 2012 A1
20120152539 Karcher Jun 2012 A1
20120167803 Luo Jul 2012 A1
20120227631 Brenneis Sep 2012 A1
20120285682 Santra et al. Nov 2012 A1
20120291674 Brenneis et al. Nov 2012 A1
20120318506 Benkley Dec 2012 A1
20120325476 Brenneis Dec 2012 A1
20120328377 Brenneis Dec 2012 A1
20130008352 Roddy Jan 2013 A1
20130048286 Morgan Feb 2013 A1
20130069755 Ikriannikov Mar 2013 A1
20130118752 Hannegan et al. May 2013 A1
20130126159 Bryan et al. May 2013 A1
20130153214 Roddy et al. Jun 2013 A1
20130157903 Benkley Jun 2013 A1
20130210685 Chatterji Aug 2013 A1
20130213642 Chatterji Aug 2013 A1
20130213643 Chatterji Aug 2013 A1
20140048266 Morgan et al. Feb 2014 A1
20140076204 Brenneis et al. Mar 2014 A1
20140123879 Karcher et al. May 2014 A1
Foreign Referenced Citations (48)
Number Date Country
2064682 Apr 1992 CA
2336077 Jan 2000 CA
2153372 Jan 2006 CA
2736148 May 2012 CA
1165849 Nov 1997 CN
1182062 May 1998 CN
1443727 Sep 2003 CN
0752048 Jan 1997 EP
0814067 Dec 1997 EP
1092693 Apr 2001 EP
1236701 Sep 2002 EP
1394137 Jul 2003 EP
1348831 Oct 2003 EP
1900703 Mar 2008 EP
2075303 Jul 2009 EP
1853680 Apr 2010 EP
1769132 Apr 2011 EP
1469954 Apr 1997 GB
2455446 Jun 2009 GB
52117316 Oct 1977 JP
55027881 Feb 1990 JP
10110487 Apr 1998 JP
1126647 Mar 2012 KR
2026959 Jan 1995 RU
2003136028 May 2005 RU
1373781 Feb 1988 SU
WO 8301443 Sep 1982 WO
WO 9321122 Oct 1993 WO
WO 9527122 Oct 1995 WO
WO 9721637 Jun 1997 WO
WO 9854108 Dec 1998 WO
WO 0063134 Jan 2000 WO
WO 03031364 Apr 2003 WO
WO 2004101951 Nov 2004 WO
WO 2004101952 Nov 2004 WO
WO 2005047212 May 2005 WO
WO 2005061846 Jul 2005 WO
WO 2006032841 Mar 2006 WO
WO 2006074946 Jul 2006 WO
WO 2007028952 Mar 2007 WO
WO 2007041841 Apr 2007 WO
WO 2007048999 May 2007 WO
WO 2007128945 Nov 2007 WO
WO 2009071962 Nov 2009 WO
WO 2009138747 Nov 2009 WO
WO 2010086592 Aug 2010 WO
2011051664 May 2011 WO
WO 2012001343 Jan 2012 WO
Non-Patent Literature Citations (228)
Entry
USPTO Final Office Action from U.S. Appl. No. 13/955,516 dated Apr. 29, 2014.
Rena Mathur, A.K. Misra and Pankaj Goel, “Influence of Wollastonite on Mechanical Properties of Concerte,” Journal of Scientific & Industrial Research, vol. 66, Dec. 2007, pp. 1029-1034.
USPTO Office Action from U.S. Appl. No. 13/955,516 dated Dec. 19, 2013.
USPTO Notice of Allowance from U.S. Appl. No. 13/180,238 dated Jan. 22, 2014.
USPTO Notice of Allowance from U.S. Appl. No. 13/851,925 dated Jan. 24, 2014.
USPTO Office Action from U.S. Appl. No. 13/851,475 dated Jan. 24, 2014.
USPTO Office Action from U.S. Appl. No. 13/620,013 dated Jan. 30, 2014.
USPTO Office Action from U.S. Appl. No. 14/079,421 dated Jan. 30, 2014.
Sugama, “Carbonation of Hydrothermally Treated Phosphate-Bonded Calcium Aluminate Cements”, pp. 1-9, 1973.
Herndon, “Setting Downhole Plugs: A State-of-the-Art”, Petroleum Engineer International, Apr. 1978.
Morgan, R.G., Suter, D.A., and Sweat, V.A., “Mathematical Analysis of a Simple Back Extrusion Rheometer,” ASAE Paper No. 79-6001, Jun. 24, 1979.
“API Specification for Materials and Testing for Well Cements”, API Spec. 10, 5th ed., pp. 7, 19-21, Jul. 1, 1980.
Sersale, “Portland-Zeolite-Cement for Minimizing Alkali-Aggregate Expansion”, 1987.
Smith, “Cementing” Society of Professional Engineers, pp. 14, 38, 1987.
Nelson, “Well Cementing”, 1990.
Smith, “Cementing” Society of Petroleum Engineers, p. 38, 1990.
“Appendix A”, API RP 13B-2, 2d ed.; pp. 6-8, Dec. 1, 1991.
Sugama, “Carbonation of Hydrothermally Treated Phosphate Bonded Calcium Aluminate Cements,” pp. 1-10, 1992.
Vinson, “Acid Removable Cement System Helps Lost Circulation in Productive Zones”, IADC/SPE 23929, Feb. 18, 1992.
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.
Janotka, “The Properties of Mortar Using Blends With Portland Cement Clinker, Zeolite Tuff and Gypsum”, 1995.
“Manufacture of supplementary cementitious materials from cement kiln dust”, Mishulovich et al., World Cement Research and Development, p. 116-120, Mar. 1996.
Sugama, “Hot Alkali Carbonation of Sodium Metaphosphate Modified Fly Ash/Calcium Aluminate Blend Hydrothermal Cements”, pp. 1661-1672, Sep. 11, 1996.
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.
Naiqian, “Study on the Suppression Effect of Natural Zeolite on Expansion of Concrete Due to Alkali-Aggregate Reaction”, 1998.
Chan, Comparative Study of the Initial Surface Absorption and Chloride Diffusion of High Performance Zeolite Silica Fume and PFA concretes, 1999.
Poon, “A Study of the Hydration of Natural Zeolite Blended Cement Pastes”, 1999.
Ding, “Extreme Vertices Design of Concrete With Combined Mineral Admixtures”, 1999.
Feng, “Zeolite Ceramiste Cellular Concrete”, 2000.
Bartlet-Gouedard, “A Non-Conventional Way of Developing Cement Slurry for Geothermal Wells”, 2001.
TXI Material Safety Data Sheet for Pressur-Seal, Oct. 2003.
“Kiln Dusts”, Apr. 14, 2005.
“Beneficial use.of Solid Waste in Maine”, Apr. 14, 2005.
“Standards for the Management of Cement Kiln Dust Waste”, Apr. 14, 2005.
“Use of Cement Kiln Dust for the Stabilization of Soils”, R. L. Parsons, et al., Apr. 14, 2005.
“Alkali-activated binders by use of industrial by-products”, Buchwald et al., Cement and concrete Research 35, p. 968-973, 2005.
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.
Adaska and Taubert, “Beneficial Uses of Cement Kiln Dust”, 2008 IEEE/PCA 50th Cement Industry technical Conference, Miami, Fl, May 19-22, 2008, pp. 1-19, 2008.
“Fly Ash Resource Center-Pozzolan,” available at http://www.rmajko.com/pozzolan.htm, Apr. 20, 2009.
Suyan, “An innovative Material for Severe Lost Circulation Control in Depleted Formations” SPE/IADC 125693, Oct. 2009.
Clinker (Cement), Wikipedia, printed from the Internet on Aug. 23, 2013, available at http://en.wikipedia.org/wiki/Clinker—(cement).
IP.com Electronic Publication, “Use of Cement Kiln Dust (CKD) in Low Temperature Cementing to Reduce Transition Times”, Sep. 25, 2013.
HES Brochure “SCR-100 Cement Retarder a Valuable Time Saver”, 1994.
HES Brochure “Halad-344 Fluid Loss Additive”, 1998.
HES Brochure “HR-5 Cement Additive”, 1998.
HES Brochure “AQF-2 Foaming Agent”, 1999.
HES Brochure “ThermaLock™ Cement for Corrosive CO2 Environments”, 1999.
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”, 1999.
HES Brochure “HR-4 Cement Retarder”, 1999.
HES Brochure “HR-7 Cement Retarder”, 1999.
HES Brochure “Pozmix A Cement Additive”, 1999.
HES Brochure “Pozmix Cement and Pozmix 140”, 1999.
HES Brochure “SCR-100™ Cement Retarder”, 1999.
HES Brochure “SCR-500L High Temp Retarder”, 2000.
HES Brochure “Halad-23 Fluid Loss Additive”, 2000.
HES Brochure “Thermatek Service”, May 2005.
HES Brochure “Micro Matrix® Cement”, Nov. 2006.
HES Brochure “VersaCem™ Cement”, Jan. 2007.
HES Brochure “Tuned Spacer™ III”, Apr. 2007.
HES Brochure “HR®-5”, Aug. 2007.
HES Brochure “Econolite™ Additive for Cement Slurries”, Aug. 2007.
HES Brochure “SSA-1™ Strength-Stabilizing Agent”, Aug. 2007.
HES Brochure “SSA-2™ Coarse Silica Flour”, Aug. 2007.
BASF Technical Bulletin “MetaMax® PA”, Aug. 2007.
HES Brochure “Silicalite™”, Aug. 2007.
HES Brochure “SCR-100™ Cement Retarder”, Aug. 2007.
HESS Pumice Products Inc., Fact Sheet for“DS-200”, “DS-325”, and “Ultrafine Grout”, Aug. 2007.
HES Brochure “Cal-Seal™ Cement Accelerator”, Aug. 2007.
HES Brochure “D-Air 4000L™ Cementing Defoamer”, Sep. 2007.
HES Brochure “WG-17 LXP™ Free-Water Control Agent”, Dec. 2007.
HES Brochure “HR®-601 Cement Retarder”, Jan. 2008.
HES Brochure “Thermatek® RSP Rapid Set Plug Service”, Mar. 2008.
HES Product Data Sheet “Baroid®”, Mar. 25, 2010.
HES Brochure “Enhancer 923™ Cement Agent”, 2010.
HES Brochure “Enhancer 923TM Agent—Successes from the Field”, 2010.
HES Brochure“Latex 3000™ Cement Additive”, Jun. 2010.
HES Brochure “Foamer 760™ Foamer/Stabilizer”, Aug. 2010.
HES Brochure “Turned® Spacer IV”, Aug. 2010.
HES Brochure “Tuned® Spacer V”, Dec. 2010.
HES Brochure “D-Air 5000™ Defoamer”, Aug. 2011.
HES Brochure “WellLife® III Cementing Service”, Jan. 2012.
HES Brochure “SA-1015™ Suspending Agent”, Mar. 2012.
HES Brochure “CFR-3™ and CFR-3L™ Dispersant”, Apr. 2012.
HES Brochure “TergoVis™ I efficiency fluid”, Apr. 2013.
HES ZoneSealant™ 2000, printed from the Internet on Sep. 9, 2013, available at http://www.halliburton.com/en-US/ps/cementing/materials-chemicals-additives/agents/foamer/zonesealant-2000-agent.page, Sep. 9, 2013.
“3M Scotchlite, Glass Bubbles Floated Product Series Product Information”, 1999.
LaFarge brochure “TerraCem™”, Aug. 2006.
LaFarge MSDS “Cement Kiln Dust”, Mar. 3, 2005.
LaFarge MSDS “LaFarge Blended Cement (cement)”, Mar. 3, 2005.
Office Action from U.S. Appl. No. 11/223,671, Dec. 15, 2005.
Office Action from U.S. Appl. No. 11/271,431, Mar. 6, 2006.
Office Action from U.S. Appl. No. 11/223,671, Mar. 31, 2006.
Office Action from U.S. Appl. No. 11/271,431, May 17, 2006.
Office Action from U.S. Appl. No. 11/271,431 (Advisory Action), Jul. 11, 2006.
Office Action from U.S. Appl. No. 11/416,563, Jul. 21, 2006.
Office Action from U.S. Appl. No. 11/403,032, Jul. 24, 2006.
Office Action from U.S. Appl. No. 11/271,431, Aug. 15, 2006.
Office Action from U.S. Appl. No. 11/440,627, Aug. 21, 2006.
Office Action from U.S. Appl. No. 11/402,741, Oct. 19, 2006.
Office Action from U.S. Appl. No. 11/484,951, Oct. 26, 2006.
Office Action from U.S. Appl. No. 11/484,951, Dec. 21, 2006.
Office Action from U.S. Appl. No. 11/223,703, Jan. 17, 2007.
Office Action from U.S. Appl. No. 11/402,741, Feb. 2, 2007.
Office Action from U.S. Appl. No. 11/223,485, Feb. 28, 2007.
Office Action from U.S. Appl. No. 11/223,669, Feb. 28, 2007.
Office Action from U.S. Appl. No. 11/271,690, Mar. 13, 2007.
Office Action from U.S. Appl. No. 11/402,741, Mar. 22, 2007.
Office Action from U.S. Appl. No. 11/223,703, Apr. 25, 2007.
Office Action from U.S. Appl. No. 11/402,741, May 29, 2007.
Office Action from U.S. Appl. No. 11/223,669, Jun. 18, 2007.
Office Action from U.S. Appl. No. 11/257,261, Aug. 10, 2007.
Office Action from U.S. Appl. No. 11/402,741, Sep. 6, 2007.
Office Action from U.S. Appl. No. 11/223,669, Oct. 9, 2007.
Office Action from U.S. Appl. No. 11/223,750, Oct. 16, 2007.
Office Action from U.S. Appl. No. 11/402,741, Oct. 24, 2007.
Office Action from U.S. Appl. No. 11/223,669, Jan. 29, 2008.
Office Action from U.S. Appl. No. 11/223,669, Apr. 8, 2008.
Office Action from U.S. Appl. No. 12/263,800, May 1, 2009.
Office Action from U.S. Appl. No. 12/283,398, Jul. 15, 2009.
Office Action from U.S. Appl. No. 12/263,800, Jul. 28, 2009.
Office Action from U.S. Appl. No. 12/420,630, Aug. 3, 2009.
Office Action from U.S. Appl. No. 12/349,676, Nov. 4, 2009.
Office Action from U.S. Appl. No. 12/606,381, Mar. 23, 2010.
Office Action from U.S. Appl. No. 12/609,993, Apr. 9, 2010.
Office Action from U.S. Appl. No. 12/609,993, Jun. 15, 2010.
Office Action from U.S. Appl. No. 12/558,097, Jun. 30, 2010.
Notice of Allowance from U.S. Appl. No. 12/609,993, Jul. 26, 2010.
Office Action from U.S. Appl. No. 12/558,097, Sep. 3, 2010.
Office Action from U.S. Appl. No. 12/844,612, Oct. 1, 2010.
Office Action from U.S. Appl. No. 12/833,189, Oct. 1, 2010.
Office Action from U.S. Appl. No. 12/844,612, Jan. 28, 2011.
Notice of Allowance from U.S. Appl. No. 12/544,915, Aug. 1, 2011.
Office Action from U.S. Appl. No. 12/844,612, Sep. 6, 2011.
Office Action from U.S. Appl. No. 12/264,010, Oct. 31, 2011.
Final Office Action from U.S. Appl. No. 12/844,612, Dec. 23, 2011.
Final Office Action from U.S. Appl. No. 12/264,010, Apr. 10, 2012.
Office Action from U.S. Appl. No. 12/844,612, Apr. 11, 2012.
Office Action from U.S. Appl. No. 13/399,913, May 15, 2012.
Office Action from U.S. Appl. No. 13/447,560, May 31, 2012.
Office Action from U.S. Appl. No. 12/821,412, Jun. 5, 2012.
Office Action from U.S. Appl. No. 12/825,004, Jun. 14, 2012.
Notice of Allowance from U.S. Appl. No. 13/447,560, Jun. 21, 2012.
Office Action from U.S. Appl. No. 13/479,476, Jul. 2, 2012.
Office Action from U.S. Appl. No. 12/975,196, Jul. 3, 2012.
Final Office Action from U.S. Appl. No. 12/844,612, Jul. 30, 2012.
Notice of Allowance from U.S. Appl. No. 13/399,913, Aug. 23, 2012.
Notice of Allowance from U.S. Appl. No. 13/535,258, Sep. 7, 2012.
Notice of Allowance from U.S. Appl. No. 13/825,004, Sep. 20, 2012.
Office Action from U.S. Appl. No. 13/477,777, Oct. 15, 2012.
Office Action from U.S. Appl. No. 13/560,406, Oct. 17, 2012.
Notice of Allowance from U.S. Appl. No. 13/844,612, Oct. 18, 2012.
Office Action from U.S. Appl. No. 13/555,624, Oct. 19, 2012.
Final Office Action from U.S. Appl. No. 12/975,196, Oct. 23, 2012.
Office Action from U.S. Appl. No. 13/431,701, Nov. 9, 2012.
Office Action from U.S. Appl. No. 13/620,163, Nov. 9, 2012.
Office Action from U.S. Appl. No. 13/606,098, Dec. 13, 2012.
Office Action from U.S. Appl. No. 13/669,149, Dec. 19, 2012.
Office Action from U.S. Appl. No. 13/620,013, Feb. 26, 2013.
Office Action from U.S. Appl. No. 12/895,436, Apr. 4, 2013.
Office Action from U.S. Appl. No. 13/725,833, Apr. 10, 2013.
Notice of Allowance from U.S. Appl. No. 13/669,149, May 13, 2013.
Notice of Allowance from U.S. Appl. No. 13/535,145, May 24, 2013.
Office Action from U.S. Appl. No. 13/620,013, May 28, 2013.
Notice of Allowance from U.S. Appl. No. 12/895,436, May 28, 2013.
Notice of Allowance from U.S. Appl. No. 13/560,406, May 29, 2013.
Final Office Action from U.S. Appl. No. 13/477,777, May 29, 2013.
Office Action from U.S. Appl. No. 13/851,925, Jun. 6, 2013.
Office Action from U.S. Appl. No. 13/889,398, Jun. 20, 2013.
Office Action from U.S. Appl. No. 13/849,309, Jul. 2, 2013.
Office Action from U.S. Appl. No. 13/851,391, Jul. 3, 2013.
Office Action from U.S. Appl. No. 13/872,063, Jul. 12, 2013.
Office Action from U.S. Appl. No. 13/767,710, Jul. 19, 2013.
Notice of Allowance from U.S. Appl. No. 13/851,391, Jul. 31, 2013.
Notice of Allowance from U.S. Appl. No. 13/889,398, Aug. 20, 2013.
Final Office Action from U.S. Appl. No. 13/851,925, Sep. 20, 2013.
Final Office Action from U.S. Appl. No. 13/767,710, Sep. 20, 2013.
Office Action from U.S. Appl. No. 13/477,777, Sep. 20, 2013.
Office Action from U.S. Appl. No. 13/180,238, Sep. 25, 2013.
Final Office Action from U.S. Appl. No. 13/620,013, Oct. 2, 2013.
Notice of Allowance from U.S. Appl. No. 13/662,111, Oct. 21, 2013.
Foreign Search Report from PCT/GB2005/001415, Sep. 9, 2005.
Foreign Search Report from PCT/GB2006/000406, Jul. 5, 2006.
Foreign Search Report from PCT/GB2006/003163, Oct. 27, 2006.
Foreign Search Report from PCT/GB2006/003160, Nov. 2, 2006.
Foreign Search Report from PCT/GB2006/003735, Dec. 1, 2006.
Foreign Search Report from PCT/GB2006/003694, Dec. 19, 2006.
Foreign Search Report from PCT/GB2006/000401, May 8, 2007.
Foreign Search Report from PCT/GB2009/000295, Feb. 3, 2009.
English language translation of USSR Patent No. RU 2026959, Jan. 20, 1995.
English language translation of Foreign Office Action for Application No. RU2008113765, Jul. 6, 2009.
English language translation of Foreign Office Action for Chinese Application No. 200680042014.3, Dec. 1, 2010.
EPO Application No. 06779194.7 Examination Report, May 29, 2009.
PCT International Search Report and Written Opinion for International Application No. PCT/GB2009/000295, Jul. 30, 2009.
PCT International Search Report and Written Opinion for International Application No. PCT/GB2009/002597, Feb. 1, 2010.
PCT International Search Report and Written Opinion for International Application No. PCT/GB2009/002598, Feb. 11, 2010.
PCT International Search Report and Written Opinion for International Application No. PCT/GB2010/000712, Jul. 26, 2010.
PCT International Preliminary Report on Patentability for International Application No. PCT/GB2009/000295, Aug. 24, 2010.
PCT International Search Report and Written Opinion for International Application No. PCT/GB2010/001986, Jan. 19, 2011.
PCT International Search Report and Written Opinion for International Application No. PCT/GB2010/002011, Feb. 4, 2011.
PCT International Preliminary Report on Patentability (Chapter 1) for International Application No. PCT/GB2009/002018, Mar. 24, 2011.
PCT International Search Report and Written Opinion for International Application No. PCT/GB2011/000933, Sep. 22, 2011.
PCT International Search Report and Written Opinion for International Application No. PCT/GB2011/001411, Jan. 27, 2012.
PCT International Search Report for International Application No. PCT/GB2011/001749, Apr. 5, 2012.
PCT International Search Report and Written Opinion for International Application No. PCT/US2012/046117, Oct. 26, 2012.
PCT International Search Report and Written Opinion for International Application No. PCT/US2013/056719, Oct. 25, 2013.
PCT International Search Report and Written Opinion for International Application No. PCT/US2013/048092, Nov. 13, 2013.
Foreign Office Action for Canadian Patent Application No. 2621835, Oct. 2, 2009.
Foreign Office Action for Canadian Patent Application No. 2621832, Oct. 5, 2009.
Foreign Office Action for Canadian Patent Application No. 2650630, Oct. 14, 2010.
Foreign Office Action for Canadian Patent Application No. 2658155, Nov. 16, 2010.
Foreign Office Action for EP Application No. 06 779 199.6, Mar. 1, 2010.
Foreign Office Action for EP Application No. 06 779 191.3, Mar. 31, 2010.
Foreign Office Action for EP Application No. 06 779 194.7, Jul. 2, 2010.
Foreign Office Action for EP Application No. 06 794 646.7, Sep. 24, 2010.
Foreign Office Action for EP Application No. 09 713 469.6, Sep. 28, 2010.
U.S. Appl. No. 13/622,821, filed Sep. 19, 2012.
International Search Report for International Application No. PCT/US2013/057213 dated Nov. 18, 2013.
Chinese Patent Application No. 200680042004.X dated Apr. 30, 2014 and translation.
The Professional Standard of the People's Republic of China, Rotary Kiln Dust Added to Cement, ZB Q 12001-84, dated Oct. 25, 1994 and translation.
Reexamination of Chinese Patent Application 200680042014.3 and translation.
USPTO Office Action for U.S. Appl. No. 13/595,493 dated Jul. 23, 2014.
Toshinori Kojima et al., Reduction of CO2 Emission from Cement Manufacturing Process by Partly Substituting Silicate for Limestone, Greenhouse Gas Control Technologies, pp. 933-938, dated 1999.
Related Publications (1)
Number Date Country
20140060389 A1 Mar 2014 US
Divisions (2)
Number Date Country
Parent 13955516 Jul 2013 US
Child 14079421 US
Parent 13399913 Feb 2012 US
Child 13477777 US
Continuation in Parts (6)
Number Date Country
Parent 13477777 May 2012 US
Child 13955516 US
Parent 13180238 Jul 2011 US
Child 13399913 US
Parent 12975196 Dec 2010 US
Child 13180238 US
Parent 12895436 Sep 2010 US
Child 13399913 US
Parent 12264010 Nov 2008 US
Child 12895436 US
Parent 11233669 Sep 2005 US
Child 12264010 US