Cement compositions comprising sub-micron alumina and associated methods

Abstract
Methods and compositions that comprise sub-micron alumina for accelerating setting of a cement composition. An embodiment includes a method of cementing in a subterranean formation. The method may comprise introducing a cement composition into the subterranean formation, wherein the cement composition comprises hydraulic cement, sub-micron alumina, and water. The method further may comprise allowing the cement composition to set in the subterranean formation. Another embodiment includes a cement composition that may comprise hydraulic cement, sub-micron alumina, and water.
Description
BACKGROUND

The present invention relates to cementing operations. More particularly, in certain embodiments, the present invention relates to cement compositions and methods of cementing in a subterranean formation that include sub-micron alumina for accelerating setting.


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, 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 and the placement of cement plugs.


The hydration of the cement in these cementing methods is a complex process because several phases may take part in the reaction simultaneously. In order to control the reaction processes to render the compositions suitable for well cementing, various additives such as retarders, strength enhancers, and accelerators may be added. However, the operating conditions for wells are becoming more challenging and demanding, and the search for new materials continues to meet these challenges. For instance, cement slurries used in well cementing often encounter problems of gaining sufficient strength in a reasonable amount of time for well operations to continue. The costs associated with wait-on-cement (“WOC”) play an important role in well cementing. This problem may be further aggravated if latex is used with the cement. Furthermore, when latex is present in cement slurries, addition of calcium salts or other salts to accelerate the setting of cement, for example, at low temperatures, can cause coagulation of the latex with resultant gelling of the cement slurries. This gelling may result in premature loss of fluidity of the cement slurry before placement in the desired location in the well bore. Latex may be used for fluid loss control, to provide resiliency to the set cement, and/or to reduce the issues associated with gas channeling. Latex-containing cement compositions, however, may have slower strength development with respect to comparable cement compositions.


SUMMARY

The present invention relates to cementing operations. More particularly, in certain embodiments, the present invention relates to cement compositions and methods of cementing in a subterranean formation that include sub-micron alumina for accelerating setting.


An embodiment of the present invention includes a method of cementing in a subterranean formation comprising: introducing a cement composition into the subterranean formation, wherein the cement composition comprises hydraulic cement, sub-micron alumina, and water; and allowing the cement composition to set in the subterranean formation.


Another embodiment of the present invention includes a method of cementing in a subterranean formation comprising: preparing a cement composition comprising hydraulic cement, sub-micron alumina for accelerating setting of the cement composition, latex, and water, wherein the sub-micron alumina has a particle size of about 150 nm to about 950 nm, wherein preparing the cement composition comprises providing a colloidal alumina dispersion comprising the sub-micron alumina in an aqueous base fluid; introducing the cement composition into a well bore in a space between the subterranean formation and a conduit disposed in the well bore; and allowing the cement composition to set.


Yet another embodiment includes a cement composition comprising hydraulic cement, sub-micron alumina, and water.


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 THE PREFERRED EMBODIMENTS

The present invention relates to cementing operations. More particularly, in certain embodiments, the present invention relates to cement compositions and methods of cementing in a subterranean formation that include sub-micron alumina for accelerating setting.


There may be several potential advantages to the methods and compositions of the present invention, only some of which may be alluded to herein. One of the many advantages of the present invention is that inclusion of sub-micron alumina in cement compositions may improve the mechanical properties of the cement composition. By way of example, inclusion of sub-micron alumina may provide accelerated setting and, thus, accelerated strength development, particularly in latex-containing cement compositions. While the methods and compositions of the present invention may be suitable for use in a wide variety of cementing operations, they may be particularly suitable for use in latex-containing cement compositions in low temperature wells, such as those having a bottomhole circulating temperature of about 40° F. to about 180° F. and, alternatively, of about 40° F. to about 125° F.


An embodiment of the cement compositions of the present invention comprises hydraulic cement, sub-micron alumina, and water. In certain embodiments, the cement compositions may further comprise latex. Those of ordinary skill in the art will appreciate that the example 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 about 4 pounds per gallon (“lb/gal”) to about 20 lb/gal. In certain embodiments, the cement compositions may have a density in the range of about 8 lb/gal to about 17 lb/gal. 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.


Embodiments of the cement compositions of the present invention comprise a hydraulic cement. Any of a variety of hydraulic cements suitable for use in subterranean cementing operations may be used in accordance with embodiments of the present invention. Suitable examples include hydraulic cements that comprise 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, pozzolana cements, gypsum cements, high-alumina-content cements, slag cements, silica/lime cements and combinations thereof. In certain embodiments, the hydraulic cement may comprise a Portland cement. The Portland cements that may be suited for use in embodiments of the present invention are classified as Class A, C, G and H cements according to American Petroleum Institute, Recommended Practice for Testing Well Cements, API Specification 10B-2 (ISO 10426-2), First edition, July 2005. In addition, in some embodiments, cements suitable for use in the present invention may include cements classified as ASTM Type I, II, or III. Belite cements also may be suitable for use in embodiments of the present invention. Belite cements typically contain belite (dicalcium silicate, C2S) as the sole or primary calcium silicate. For example, belite cement may comprise belite in an amount of at least about 50% by weight of calcium silicates. By way of further example, a belite cement may comprise belite in an amount of at least about 80% by weight of calcium silicates and, alternatively, in an amount of at least about 95% by weight of calcium silicates. However, due to their slower rate of strength development, belite cements may not be suitable for certain applications, such as in latex-containing cement compositions.


Embodiments of the cement compositions of the present invention further comprise sub-micron alumina. As used herein, sub-micron alumina is defined as alumina having any one of the structural features or dimensions, for example, length, width, thickness, or diameter, of greater than about 100 nanometers (“nm”) and less than about 1 micron or, in a preferred range, of greater than about 150 nm to about 950 nm. For example, the sub-micron alumina may have a particle size in the range of about 200 nm to about 800 nm and, alternatively, in the range of about 400 nm to about 500 nm. In contrast to sub-micron alumina, it should be understood that nano-alumina has a particle size of less than about 100 nm. Sub-micron alumina, however, may be more useful than nano-alumina due, for example, to its low cost as compared with nano-materials. It should be noted that the sub-micron alumina may be used in combination with differently sized particles of alumina, in accordance with present embodiments. For example, alumina with particle sizes greater than about 1 micron and/or less than about 100 nm may be included in a cement composition in accordance with present embodiments.


As used herein, “particle size” refers to volume surface mean diameter (“DS”) which is related to the specific surface area. Volume surface mean diameter may be defined by the following formula: DS=6/(ΦSAwρp) where ΦS=Sphericity; Aw=Specific surface area and ρp=Particle density. It should be understood that the particle size of the sub-micron alumina may vary based on the measurement technique, sample preparation, and sample conditions (e.g., temperature, concentration, etc.). One technique for measuring particle size of the sub-micron alumina at room temperature (approx. 80° F.) includes dispersing the particle in a suitable solvent (such as chloroform, dichloroethane, acetone, methanol, ethanol, water, etc.) by sonification and proper dilution. A dispersing agent may be used to deagglomerate the particles, if needed. The diluted, dispersed solution may then be placed on a carbon-coated copper grid with 300 mesh size by using a micropipette. It may then be dried and examined by Transmission electron microscopy (TEM). The particle size distribution may be obtained with high accuracy using an appropriate computation technique. By way of example, TEM image processing may use image-processing software such as Image-Pro® Plus software from Media Cybernetics to determine the particle size. Another example technique involves use of calibrated drawing tools in Digital Micrograph software followed by statistical analysis of the data with Kaleida-Graph software to determine the particle size.


Different types of sub-micron alumina may be used in accordance with embodiments of the present invention. For example, the sub-micron alumina may be provided as a colloidal alumina dispersion that comprises sub-micron alumina particles suspended in base fluid such as water. Embodiments of the present invention also may include sub-micron alumina in a dry, free-flowing state. Alternatively, discrete particles of the sub-micron alumina may be agglomerated to form a cohesive mass. The agglomerated sub-micron alumina may then be included in the cement composition in embodiments of the present invention. It should be understood that the agglomerated sub-micron alumina generally should disperse into discrete particles of sub-micron alumina after mixing with the cement composition, either immediately after a delay period. Alternately, a suitable dispersant, for example an anionic acrylate polymer or suitable surfactants, capable of dispersing agglomerated alumina into discrete particles of sub-micron alumina may be added to mix water, followed by solid alumina or a dispersion in a base fluid, and finally solid cement blend. Alternately, solid alumina powder may be coated with a dispersing compound capable of dispersing agglomerated alumina into discrete particles of sub-micron alumina and used as a solid additive to cement blend or to mix water.


Sub-micron alumina differs from larger-sized particulate materials (e.g., larger-sized particulate alumina) particular that may be included cement compositions due to its high surface to volume ratio. The area of the interface between the cement matrix and the sub-micron alumina is typically an order of magnitude greater than that in compositions containing larger-sized composite materials. Due to their high surface energy, the sub-micron alumina may exhibit improved properties as compared to larger-sized materials.


It is now recognized that the sub-micron alumina utilized with present embodiments, may have an impact on certain physical characteristics of the cement compositions. For example, relative to cement compositions that do not contain sub-micron alumina, inclusion of sub-micron alumina may provide for more rapid strength development as well as accelerated setting. More particularly, inclusion of a colloidal sub-micron alumina dispersion in a cement slurry in an amount of about 0.2 gallons per 94-pound sack of cement (“gps”) may increase the strengths from about 20% to about 65% after twenty-four hours compared to an identical slurry without sub-micron alumina, in accordance with embodiments of the present invention. In addition, inclusion of a colloidal sub-micron alumina dispersion in a latex-containing composition in an amount of 0.05 gps to about 0.2 gps may increase strength by at least about 85% after forty-eight hours with potentially up to 2.5 times higher strength after forty-eight hours. The colloidal alumina dispersion may contain, for example, about 10% to about 30% dispersed sub-micron alumina phase (e.g., 400 nm to 500 nm) by weight.


Accordingly, a cement composition in accordance with present embodiments may comprise a sufficient amount of the sub-micron alumina to provide the desired characteristics (e.g., strength development) for the cement composition. In some embodiments, the sub-micron alumina may be present in the cement composition in an amount in the range of about 0.1% to about 10% by weight of the cement on a dry basis (“bwoc”) (e.g., about 0.5%, about 1%, about 2%, about 4%, about 6%, about 8%, etc.). More particularly, the sub-micron alumina may be present in embodiments of the cement composition in an amount in the range of about 0.5% to about 5% bwoc.


The water used in 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% bwoc. In certain embodiments, the water may be present in an amount in the range of about 35% to about 70% bwoc.


Moreover, embodiments of the cement compositions of the present invention also may comprise latex. As will be understood by those skilled in the art, the latex may comprise any of a variety of rubber materials that are commercially available in latex form, either as aqueous emulsions or dry powders. Suitable rubber materials include natural rubber (e.g., cis-1,4-polyisoprene), modified natural rubber, synthetic rubber, and combinations thereof. Synthetic rubber of various types may be utilized, including ethylene-propylene rubbers, styrene-butadiene rubbers, nitrile rubbers, nitrile butadiene rubbers, butyl rubber, neoprene rubber, polybutadiene rubbers, acrylonitrile-styrene-butadiene rubber, polyisoprene rubber, and AMPS-styrene-butadiene rubber, combinations thereof. As used herein, the term “AMPS” refers to 2-acrylamido-2-methylpropanesulfonic acid and salts thereof. In certain embodiments, the synthetic rubber may comprise AMPS in an amount ranging from about 7.5% to about 10%, styrene in an amount ranging from about 30% to about 70% and butadiene in an amount ranging from about 30% to about 70%. Examples of suitable AMPS-styrene-butadiene rubbers are described in more detail in U.S. Pat. Nos. 6,488,764 and 6,184,287, the entire disclosures of which are incorporated herein by reference. Those of ordinary skill in the art will appreciate that other types of synthetic rubbers are also encompassed within the present invention.


In certain embodiments, the latex comprises an aqueous emulsion that comprises styrene-butadiene rubber. As will be appreciated, the aqueous phase of the emulsion comprises an aqueous colloidal dispersion of the styrene-butadiene copolymer. Moreover, in addition to the dispersed styrene-butadiene copolymer, the emulsion may comprise water in the range of about 40% to about 70% by weight of the emulsion and small quantities of an emulsifier, polymerization catalysts, chain modifying agents, and the like. As will be appreciated, styrene-butadiene latex is often produced as a terpolymer emulsion that may include a third monomer to assist in stabilizing the emulsion. Non-ionic groups which exhibit steric effects and which contain long ethoxylate or hydrocarbon tails also may be present.


In accordance with embodiments of the present invention, the weight ratio of the styrene to the butadiene in the latex may be in the range of about 10:90 to about 90:10. In some embodiments, the weight ratio of the styrene to the butadiene in the emulsion may be in the range of about 20:80 to about 80:20. An example of a suitable styrene-butadiene latex has a styrene-to-butadiene weight ratio of about 25:75 and comprises water in an amount of about 50% by weight of the emulsion. Such a styrene-butadiene latex is available from Halliburton Energy Services, Inc., Duncan, Okla., under the name Latex 2000™ cement additive. Another example of a suitable styrene-butadiene latex has a styrene-to-butadiene weight ratio of about 30:70.


Where used, the latex may be provided in the cement compositions of the present invention in an amount sufficient for the desired application. In some embodiments, the latex may be included in the cement compositions in an amount in the range of about 2% to about 45% bwoc. In some embodiments, the latex may be included in the cement compositions in an amount in the range of about 5% to about 27% bwoc.


Embodiments of the cement compositions of the present invention also may comprise a latex stabilizer. Among other things, the latex stabilizer may be included in embodiments of the cement compositions for preventing the cement compositions from prematurely coagulating. Suitable latex stabilizers may include a surfactant or combination of surfactants for preventing the premature inversion of the latex emulsion. Examples of suitable latex stabilizers include, but are not limited to, surfactant molecules containing ethoxylated alkyl sulfonates and sulfates. Additional examples of suitable latex stabilizing surfactants which are suitable for this purpose may have the formula R-Ph-O(OCH2CH2)mOH where R contains an alkyl group of from about 5 to about 30 carbon atoms, Ph contains a phenyl group, and m is an integer having value between 5 to 50. An example of a surfactant of this formula is ethoxylated nonylphenyl containing in the range of about 20 to about 30 moles of ethylene oxide. Another example of a suitable surfactant is a salt having the formula R1(R2O)nSO3X where R1 contains an alkyl group having 5 to 20 carbon atoms, R2 contains the group —CH2—CH2—, n is an integer having value in between 10 to 40, and X is any suitable cation. An example of surfactant of this formula is the sodium salt of a sulfonated compound derived by reacting a C12-15 alcohol with about 15 moles of ethylene oxide having the formula H(CH2)12-15(CH2CH2O)15SO3Na. Specific examples of suitable latex stabilizers include Stabilizer 434B™ latex stabilizer, Stabilizer 434C™ latex stabilizer, and Stabilizer 434D™ latex stabilizer, which are available from Halliburton Energy Services, Inc. While embodiments of the present invention encompass a wide variety of different latex stabilizers and amounts thereof that may be included in the cement compositions of the present invention depending on the particular latex used and other factors, the latex stabilizer may be included in embodiments of the cement compositions in an amount in the range of about 0% to about 30% by weight of the aqueous latex in the cement composition and, alternatively, about 10% to about 20% by weight.


Other additives suitable for use in subterranean cementing operations also may be added to embodiments of the cement compositions, in accordance with embodiments of the present invention. Examples of such additives include, but are not limited to, strength-retrogression additives, set accelerators, set retarders, weighting agents, lightweight additives, gas-generating additives, mechanical property enhancing additives, lost-circulation materials, filtration-control additives, dispersants, fluid loss control additives, defoaming agents, foaming agents, thixotropic additives, nano-particles, and combinations thereof. By way of example, the cement composition may be a foamed cement composition further comprising a foaming agent and a gas. Specific examples of these, and other, additives include crystalline silica, amorphous silica, fumed silica, salts, fibers, hydratable clays, calcined shale, vitrified shale, microspheres, fly ash, slag, diatomaceous earth, metakaolin, rice husk ash, natural pozzolan, zeolite, cement kiln dust, lime, elastomers, resins, nano-clays (e.g., naturally occurring, organically modified), nano-silica, nano-zinc oxide, nano-boron, nano-iron oxide, nano-zirconium oxide, nano-magnesium oxide, nano-barite, 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.


An example of a cement composition of the present invention comprises Portland cement, colloidal alumina dispersions in an aqueous base fluid in an amount of about 0.05 gps to about 0.2 gps, and water. The colloidal alumina dispersions may comprise sub-micron alumina in an amount of about 10% to about 30% by weight of the dispersions. Embodiments of the example cement composition further may comprise an aqueous latex, such as styrene-butadiene latex or AMPS-styrene-butadiene latex. Additional additives may include a defoaming agent (such as D-AIR 3000L™ defoamer), a cement set retarder (such as HR-6L retarder), and a cement dispersant (such as CFR-3L dispersant).


Another example of a cement composition of the present invention comprises Portland cement, colloidal alumina dispersions in an aqueous base fluid in an amount of about 0.05 gps to about 0.2 gps, styrene-butadiene latex in an amount of about 1.5 gps, and water. The colloidal alumina dispersions may comprise sub-micron alumina in an amount of about 10% to about 30% by weight of the dispersions. Embodiments of the example cement composition further may comprise an aqueous latex, such as styrene-butadiene latex or AMPS-styrene-butadiene latex. Additional additives may include a defoaming agent (such as D-AIR 3000L™ defoamer), a latex stabilizer (such as Stabilizer 434D™ latex stabilizer), a cement set retarder (such as HR-6L retarder), and a cement dispersant (such as CFR-3L dispersant).


As will be appreciated by those of ordinary skill in the art, embodiments of the cement compositions of the present invention may be used in a variety of subterranean applications, including primary and remedial cementing. Embodiments of the cement compositions may be introduced into a subterranean formation and allowed to set therein. Embodiments of the cement compositions may comprise, for example, cement, sub-micron alumina, and water. Embodiments of the cement compositions further may comprise latex in certain applications.


In primary cementing embodiments, for example, a cement composition may be introduced into a space between a subterranean formation and a conduit (e.g., 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 conduit. Among other things, the set cement composition may form a barrier, preventing the migration of fluids in the well bore. The set cement composition also may, for example, support the conduit in the well bore.


In remedial cementing embodiments, a cement composition may be used, for example, in squeeze-cementing operations or in the placement of cement plugs. By way of example, the cement composition may be placed in a well bore to plug a void or crack in the conduit or the cement sheath or a microannulus between the cement sheath and the conduit.


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


Example 1

This example was performed to analyze the effect of including sub-micron alumina in a cement composition. For this example, six different slurries were prepared. The cement compositions were then tested to determine their rate of strength development and thickening times. As set forth below, the respective test results for the six different slurries demonstrate that inclusion of sub-micron alumina in the slurry provides faster early strength development and shortened thickening times.


Slurries 1-6 each included Portland Class H cement, 0.05 gps of a defoamer (D-AIR 3000L™ available from Halliburton Energy Services, Inc.), and sufficient water to provide the density listed in the table below. Slurries 2, 4, and 6 also included a colloidal alumina dispersion in an amount of 0.2 gps. The colloidal alumina dispersion was supplied by Bee Chems, India and contained sub-micron alumina (400 nm to 500 nm) in an aqueous base fluid in an amount of about 20% by weight.


After the six slurries were prepared, tests were performed to determine various physical characteristics associated with inclusion of the sub-micron alumina in each of the slurries. One of these tests was performed to determine the rate of strength development for each of the slurries. An ultrasonic cement analyzer (“UCA”) available from FANN Instrument Company, USA (Controller Model 304) was used to determine the compressive strength rate as a function of time. The rate of strength development was calculated as the slope of the initial linear part (starting from the onset of the strength development) of the compressive strength versus time graph. Additionally, the UCA was also used to determine the compressive strength of the slurries after twenty-four hours and the time for the slurries to develop a compressive strength of 500 psi. The thickening time associated with each slurry was determined by performing a thickening-time test at 125° F. in accordance with API Recommended Practice 10B-2. The thickening time for each slurry was defined as time required for the respective slurry to reach a consistency of 70 Bearden units (Bc) at 125° F.


The results of these tests are provided in the table below.









TABLE 1







Effect of Sub-Micron Alumina on Development of High-Early


Strength and Thickening Times in Latex-Containing Slurries











Colloidal
UCA at 100° F.
















Sub-Micron
Rate of


Thickening



Slurry
Alumina
Strength
Time for
Strength
Time @ 5160 psi



Density
Dispersion
Development
500 psi
@ 24 hrs
and 125° F.


Slurry
(lb/gal)
(gps)
(psi/hr)
(hr:min)
(psi)
(hr:min)
















1
13

28
23:29
510
10:45 


2
13
0.2
36
17:39
613
1:37


3
14

35
18:31
657
4:10


4
14
0.2
80
10:38
1189
2:04


5
16.41

134
 9:17
2065
2:03


6
16.41
0.2
263
 5:29
3414
1:12






1Gelling behavior was observed for this density.







Table 1 illustrates the development of high-early strength for slurries containing sub-micron alumina. In particular, as compared to slurries without sub-micron alumina, the compressive strength obtained in twenty-four hours increased dramatically for the slurries containing sub-micron alumina with the increase in compressive strength from 20% to 65%, depending on, for example, slurry density. Moreover, the time required for the development of 500 psi was considerably shorter as compared to the slurries without sub-micron alumina. Moreover, the thickening times in Table 1 also indicate that slurries containing sub-micron alumina should also have shorter thickening times, and yet of sufficient duration to meet placement requirements, suggesting that sub-micron alumina may act as a set accelerator, in addition to acting as a strength enhancer and as an additive for increasing rates of strength development.


Example 2

This example was performed to compare sub-micron alumina with a conventional cement set accelerator (Econolite™ additive). For this example, four different slurries were prepared. The cement compositions were then tested to determine their rate of strength development and thickening times. As set forth below, the respective test results for the four different slurries demonstrate that inclusion of sub-micron alumina in the slurry provides comparable results to the Econolite™ additive at a reduced quantity.


Slurries 7-10 each included Portland Class H cement, 0.05 gps of a defoamer (D-AIR 3000L™ available from Halliburton Energy Services, Inc.), and sufficient water to provide the density listed in the table below. Slurry 8 also included Econolite™ additive, available from Halliburton Energy Services, Inc. Slurries 9-10 also included a colloidal alumina dispersion supplied by Bee Chems, India. The colloidal alumina dispersion contained sub-micron alumina (400 nm to 500 nm) in an aqueous base fluid in an amount of about 20% by weight.


After the four slurries were prepared, tests were performed to compare various physical characteristics of each of the slurries. One of these tests was performed to determine the rate of strength development for each of the slurries. A UCA was used to determine the compressive strength rate as a function of time. The rate of strength development was calculated as the slope of the initial linear part (starting from the onset of the strength development) of the Compressive strength versus Time graph. Additionally, the UCA was used to determine the compressive strength of the slurries after twenty-four hours and the time for the slurries to develop a compressive strength of 500 psi. The thickening time associated with each cement slurry was determined by performing a thickening-time test at 125° F. in accordance with API Recommended Practice 10B-2. The thickening time for each slurry was defined as the time required for the respective slurry to reach a consistency of 70 Bc at 125° F.


The results of these tests are provided in the table below.









TABLE 2







Comparison of Sub-Micron Alumina With a Conventional Cement Set Accelerator










UCA at 100° F.












Rate of

Thick. Time














Slurry
Accelerator
Strength
Time for
Strength
@ 5160 psi















Density

Amt
Development
500 psi
@ 24 hrs
and 125° F.














Slurry
(lb/gal)
Type
(gps)
(psi/hr)
(hr:min)
(psi)
(hr:min)

















7
12.5


30
21:08
547
n/d1


8
12.5
Econolite ™
0.7
14
25:19
434
1:25




Additive


9
12.5
Colloidal
1.02
33
35:19
445
3:27




Sub-Micron




Alumina




Dispersion


10
12.5
Colloidal
0.2
29
26:12
398
1:27




Sub-Micron




Alumina




Dispersion






1The thickening time for Slurry 7 could not be measured precisely.




2The % solids in Slurry 9 was equivalent to the Econolite ™ in Slurry 8.







Table 2 illustrates that sub-micron alumina provides better strength development rates and reasonable thickening times when compared with a conventional cement set accelerator. More particularly, at the same slurry density, a lower quantity of sub-micron alumina provided equivalent results to that of the Econolite™ additive.


Example 3

This example was performed to compare sub-micron alumina with another conventional cement set accelerator (calcium chloride). For this example, three different slurries were prepared. The cement compositions were then tested to determine their rate of strength development and thickening times. As set forth below, the respective test results for the three different slurries demonstrate that inclusion of sub-micron alumina in the slurry provides comparable results to the calcium chloride at a lower quantity.


Slurries 11-13 each included Portland Class H cement, 0.05 gps of a defoamer (D-AIR 3000L™ available from Halliburton Energy Services, Inc.), and sufficient water to provide the density listed in the table below. Slurry 12 also included calcium chloride. Slurries 13 also included a colloidal alumina dispersion in an amount of 0.2 gps. The colloidal alumina dispersion was supplied by Bee Chems, India and contained sub-micron alumina (400 nm to 500 nm) in an aqueous base fluid in an amount of about 20% by weight.


After the three slurries were prepared, tests were performed to compare various physical characteristics of each of the slurries. One of these tests was performed to determine the rate of strength development for each of the slurries. A UCA was used to determine the compressive strength rate as a function of time. The rate of strength development was calculated as the slope of the initial linear part (starting from the onset of the strength development) of the Compressive strength versus Time graph. Additionally, the UCA was also used to determine the compressive strength of the slurries after twenty-four hours and the time for the slurries to develop a compressive strength of 500 psi. The thickening time associated with each cement slurry was determined by performing a thickening-time test at 125° F. in accordance with API Recommended Practice 10B-2. The thickening time for each slurry was defined as the time required for the respective slurry to reach a consistency of 70 Bc at 125° F.


The results of these tests are provided in the table below.









TABLE 3







Comparison of Sub-Micron Alumina With a Conventional Cement Set Accelerator










UCA at 100° F.



















Rate of


Thick. Time



Slurry


Strength
Time for
Strength
@ 5160 psi














Density
Accelerator
Development
500 psi
@ 24 hrs
and 125° F.














Slurry
(lb/gal)1
Type
Amt
(psi/hr)
(hr:min)
(psi)
(hr:min)





11
16.4


134
9:17
2065
2:03


12
16.4
Calcium
2% bwoc
225
3:36
3400
00:49 




Chloride


13
16.4
Colloidal
0.2 gps
263
5:29
3414
1:12




Sub-Micron




Alumina




Dispersion






1At 16.4 lb/gal some gelling was noticed, regardless of the cement set accelerator.







Table 3 illustrates that sub-micron alumina provides comparable strength development rates and reasonable thickening times when compared with a conventional cement set accelerator. More particularly, at the same slurry density, a lower quantity of sub-micron alumina provided equivalent results to that of calcium chloride.


Example 4

This example was performed to analyze the effect of including sub-micron alumina in latex-containing cement compositions. For this example, four different slurries were prepared. The cement compositions were then tested to determine their rate of strength development and thickening times. As set forth below, the respective test results for the four different slurries demonstrate that inclusion of sub-micron alumina in the slurry provides higher early strengths and faster strength development rates with reasonable thickening times.


Slurries 14-17 each contained Portland Class H cement, latex in an amount of 1.5 gps, and a colloidal alumina dispersion in an amount ranging from 0 gps to 0.2 gps. Sufficient water was included in the slurries to provide a density of 16.4 lb/gal. Additional additives present in each slurry were D-AIR 3000L™ defoamer in an amount of 0.05 gps, Stabilizer 434D™ latex stabilizer in an amount of 0.2 gps, HR®-6L cement set retarder in an amount of 0.05 gps, and CFR-3L™ dispersant in an amount of 0.143 gps. The latex included in the slurries was Latex 2000™ cement additive having a particle size ranging from 150 nm to 200 nm. The colloidal alumina dispersion was supplied by Bee Chems, India and contained sub-micron alumina (400 nm to 500 nm) in an aqueous base fluid in an amount of about 20% by weight.


After the four slurries were prepared, tests were performed to compare various physical characteristics of each of the slurries. One of these tests was performed to determine the rate of strength development for each of the slurries. A UCA was used to determine the compressive strength rate as a function of time. The rate of strength development was calculated as the slope of the initial linear part (starting from the onset of the strength development) of the Compressive strength versus Time graph. Additionally, the UCA was also used to determine the compressive strength of the slurries after twenty-four and forty-eight hours. The thickening time associated with each cement slurry was determined by performing a thickening-time test in accordance with API Recommended Practice 10B-2. The thickening time for each slurry was based on the respective slurry reaching a consistency of 70 Bc at 80° F.


The results of these tests are provided in the table below.









TABLE 4







Effect of Sub-Micron Alumina Loading on Strength Development


and Thickening Times on Slurries Containing Latex












Colloidal

UCA

















Sub-Micron

Rate of







Alumina

Strength
Strength
Strength
Thick. Time



Latex
Dispersion
Temp.
Development
@ 24 hrs
@ 48 hrs
@ 80° F.


Slurry
(gps)
(gps)
(° F.)
(psi/hr)
(psi)
(psi)
(hr:min)

















14
1.5
0.0
80
111
0
1503
28:53


15
1.5
0.05
80
145
0
2797
26:30


16
1.5
0.1
80
144
573
3159
14:26


17
1.5
0.2
80
168
1495
4019
 6:56









Table 4 illustrates that there were significant increases in twenty-four hour and forty-eight hour compressive strength values as the concentration of sub-micron alumina was increased from 0 gps to 0.2 gps. As compared to the neat latex slurry, the forty-eight hour compressive strength increased almost 2.5 times by addition of 0.2 gps of sub-micron alumina. It should be noted that the test temperature was 80° F. At 0.2 gps of sub-micron alumina, the slurry had a reasonable thickening time of 6 hours and 56 minutes. The neat latex slurry at this temperature took more than 28 hours to reach 70 Bc. The results indicate that sub-micron alumina when added to latex-containing cement slurries acts as a set accelerator, a strength enhancer and provides for increased rates of strength development at low temperatures.


Example 5

This example was performed to analyze the effect of temperature variation on the rate of strength development for slurries containing latex and sub-micron alumina. For this example, three different slurries were prepared. The cement compositions were then tested to determine their rate of strength development and thickening times. As set forth below, the respective test results for the three different slurries demonstrate that sub-micron alumina can be used as an accelerator for latex-containing cement slurries at low temperatures.


Slurries 18-20 each contained Portland Class H cement, latex in an amount of 1.5 gps, and a colloidal alumina dispersion in an amount of about 0.2 gps. Sufficient water was included in the slurries to provide a density of 16.4 lb/gal. Additional additives present in each slurry were D-AIR 3000L™ defoamer in an amount of 0.05 gps, Stabilizer 434D™ latex stabilizer in an amount of 0.2 gps, HR®-6L cement set retarder in an amount of 0.05 gps, and CFR-3L™ dispersant in an amount of 0.143 gps. The latex included in the slurries was Latex 2000™ cement additive having a particle size ranging from 150 nm to 200 nm. The colloidal alumina dispersion was supplied by Bee Chems, India and contained sub-micron alumina (400 nm to 500 nm) in an aqueous base fluid in an amount of about 20% by weight.


After the three slurries were prepared, tests were performed to determine various physical characteristics associated with varying the temperature on slurries containing latex and sub-micron alumina. One of these tests was performed to determine the rate of strength development for each of the slurries. A UCA was used to determine the compressive strength rate as a function of time. The rate of strength development was calculated as the slope of the initial linear part (starting from the onset of the strength development) of the Compressive strength versus Time graph. Additionally, the UCA was also used to determine the compressive strength of the slurries after twenty-four, forty-eight hours, seventy-two hours. The forty-eight and seventy-two hour compressive strength values were not determined for Slurry 20 because it had higher strength at twenty-four hours. The seventy-two hour compressive strength value was not determined for Slurry 19 because it had higher strength at forth-eight hours. The thickening time associated with each cement slurry was determined by performing a thickening-time test in accordance with API Recommended Practice 10B-2. The thickening time for each slurry was based on the respective slurry reaching a consistency of 70 Bc at 80° F.


The results of these tests are provided in the table below.









TABLE 5







Effect of Temperature on Strength Development for


Slurries Containing Latex and Sub-Micron Alumina












Colloidal

UCA


















Sub-Micron

Rate of








Alumina

Strength
Strength
Strength
Strength
Thickening



Latex
Dispersion
Temp.
Development
@ 24 hrs
@ 48 hrs
@ 72 hrs
Time @ 80° F.


Slurry
(gps)
(gps)
(° F.)
(psi/hr)
(psi)
(psi)
(psi)
(hr:min)


















18
1.5
0.2
40
90
58
61.7
1014
18:41 


19
1.5
0.2
80
168
195
4019
not
6:56









measured


20
1.5
0.2
120
297
2572
not
not
1:29








measured
measured









Table 5 illustrates that sub-micron alumina may be a suitable set accelerator at low temperatures for latex-containing slurries. Even at a low temperature of 40° F., a compressive strength of 1014 psi was obtained in seventy-two hours for Slurry 18. The rate of strength development increased as the temperature increased from 40° F. to 120° F. Thickening times decreased as the temperature was increased.


Example 6

This example was performed to compare the performance of sub-micron alumina with nano-silica and sub-micron calcium carbonate. For this example, four different slurries were prepared. The cement compositions were then tested to determine their rate of strength development and thickening times. As set forth below, the respective test results for the four different slurries demonstrate that inclusion of sub-micron alumina in the slurry provides higher compressive strength with reasonable thickening times.


Slurries 21-24 each included Portland Class H cement, latex in an amount of 1.5 gps, and sufficient water to provide a density of 16.4 lb/gal. Additional additives present in each slurry were D-AIR 3000L™ defoamer in an amount of 0.05 gps, Stabilizer 434D™ latex stabilizer in an amount of 0.2 gps, HR®-6L cement set retarder in an amount of 0.05 gps, and CFR-3L™ dispersant in an amount of 0.143 gps. Slurry 22 also included a colloidal nano-silica dispersion (0.2 gps) supplied by Bee Chems, India, under the trade name CemSyn LP (6 nm). The colloidal nano-silica dispersion contained nano-silica (6 nm) in an amount of about 15% by weight. Slurry 23 also included a colloidal calcium carbonate dispersion (0.3 gps) supplied by Revertex-KA Latex (India) Private Limited. The colloidal calcium carbonate dispersion contained sub-micron calcium carbonate (200 nm to 800 nm) in an amount of 75.5% by weight. Slurry 24 also included a colloidal alumina dispersion (0.2 gps) supplied by Bee Chems, India. The colloidal alumina dispersion contained sub-micron alumina (400 nm to 500 nm) in an aqueous base fluid in an amount of about 20% by weight.


After the four slurries were prepared, tests were performed to compare various physical characteristics of each of the slurries. A UCA was used to determine the compressive strength rate as a function of time. The rate of strength development was calculated as the slope of the initial linear part (starting from the onset of the strength development) of the Compressive strength versus Time graph. Additionally, the UCA was also used to determine the compressive strength of the slurries after forty-eight hours. The thickening time associated with each cement slurry was determined by performing a thickening-time test in accordance with API Recommended Practice 10B-2. The thickening time for each slurry was based on the respective slurry reaching a consistency of 70 Bc at 125° F.


The results of these tests are provided in the table below.









TABLE 6







Comparison of Sub-Micron Alumina With Nano-Silica


and Sub-Micron CaCO3 for Latex-Containing Slurries










UCA












Rate of

Thick Time



Strength
Strength
at 5160 psi














Latex
Colloidal Dispersion
Temp
Development
@ 48 hrs
and 125° F.














Slurry
(gps)
Type
Amt1
(° F.)
(psi/hr)
(psi)
(hr:min)





21
1.5


80
111
1503
28:53


22
1.5
Nano-Silica
0.2 gps
80
134
2933
15:26


23
1.5
Sub-Micron
0.3 gps
80
182
2274
19:16




CaCO3


24
1.5
Sub-Micron
0.2 gps
80
168
4019
 6:56




Alumina






1This comparison was performed using a loading of the nano-silica, sub-micron calcium carbonate, or sub-micron alumina that was found to be best for slurry performance.







Accordingly, Table 6 illustrates that sub-micron alumina provides higher strengths and faster set acceleration times when compared with nano-sized silica and sub-micron calcium carbonate, especially at 80° F.


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. While 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. 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. 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 in a subterranean formation: providing a hydraulic cement,providing sub-micron alumina particles,preparing a cement composition comprising the hydraulic cement, the sub-micron alumina particles, and water, wherein the sub-micron alumina particles have a particle size in a range of from about 150 nm to about 950 nm, and wherein the sub-micron alumina particles are present in an amount in a range of from 0.1% to about 10% by weight of the hydraulic cement on a dry basis;introducing the cement composition into a subterranean formation; andallowing the cement composition to set in the subterranean formation.
  • 2. The method of claim 1 wherein the hydraulic cement comprises at least one hydraulic cement selected from the group consisting of a Portland cement, a pozzolana cement, a gypsum cement, a high-alumina-content cement, a slag cement, a silica/lime cement, and any combination thereof.
  • 3. The method of claim 1 wherein the cement composition comprises belite in an amount from 0.1% to about 50% by weight of calcium silicates in the cement composition.
  • 4. The method of claim 1 wherein the cement composition comprises a colloidal alumina dispersion comprising sub-micron alumina particles suspended in a base fluid.
  • 5. The method of claim 1 comprising providing the sub-micron alumina particles in a dry, free-flowing form.
  • 6. The method of claim 1 wherein the sub-micron alumina particles have a particle size in the range of about 400 nm to about 500 nm.
  • 7. The method of claim 1 wherein the sub-micron alumina particles are present in the cement composition in an amount in the range of about 0.5% to about 5% by weight of the hydraulic cement on a dry basis.
  • 8. The method of claim 1 wherein the cement composition further comprises a latex.
  • 9. The method of claim 8 wherein the latex comprises at least one rubber material selected from the group an ethylene-propylene rubber, a styrene-butadiene rubber, a nitrile rubber, a nitrile butadiene rubber, a butyl rubber, a neoprene rubber, a polybutadiene rubber, an acrylonitrile-styrene-butadiene rubber, a polyisoprene rubber, and any combination thereof.
  • 10. The method of claim 1 wherein the cement composition further comprises at least one additive selected from the group consisting of a latex stabilizer, 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 filtration-control additive, a fluid loss control additive, a dispersant, a defoaming agent, a foaming agent, a thixotropic additive, and any combination thereof.
  • 11. The method of claim 1 wherein the cement composition further comprises at least one additive selected from the group consisting of a gas, crystalline silica, amorphous silica, fumed silica, a salt, a fiber, a hydratable clay, calcined shale, vitrified shale, a microsphere, fly ash, slag, diatomaceous earth, metakaolin, rice husk ash, a natural pozzolan, zeolite, cement kiln dust, lime, an elastomer, a resin, and any combination thereof.
  • 12. The method of claim 1 wherein introducing the cement composition into the subterranean formation comprises introducing the cement composition into a well bore in a space between the subterranean formation and a conduit disposed in the well bore.
  • 13. The method of claim 1 wherein introducing the cement composition into the subterranean formation comprises introducing the cement composition into a well bore having a bottomhole circulating temperature of about 40° F. to about 180° F.
  • 14. A method of cementing in a subterranean formation: providing a hydraulic cement,providing sub-micron alumina particles,preparing a cement composition comprising the hydraulic cement, the sub-micron alumina particles for accelerating setting of the cement composition, latex, and water, wherein the sub-micron alumina particles have a particle size of about 150 nm to about 950 nm, wherein preparing the cement composition comprises providing a colloidal alumina dispersion comprising the sub-micron alumina particles in an aqueous base fluid;introducing the cement composition into a well bore in a space between the subterranean formation and a conduit disposed in the well bore; andallowing the cement composition to set.
  • 15. The method of claim 14 wherein the latex comprises a styrene-butadiene latex.
  • 16. The method of claim 14 wherein the sub-micron alumina particles are present in the cement composition in an amount in the range of about 0.1% to about 10% by weight of the hydraulic cement on a dry basis, and wherein the sub-micron alumina particles have a particle size of about 400 nm to about 500 nm.
  • 17. The method of claim 14 wherein the cement composition further comprises at least one additive selected from the group consisting of a latex stabilizer, 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 filtration-control additive, a fluid loss control additive, a dispersant, a defoaming agent, a foaming agent, a thixotropic additive, and any combination thereof.
  • 18. The method of claim 14 wherein the cement composition further comprises at least one additive selected from the group consisting of crystalline silica, amorphous silica, fumed silica, a salt, a fiber, a hydratable clay, calcined shale, vitrified shale, a microsphere, fly ash, slag, diatomaceous earth, metakaolin, rice husk ash, natural pozzolan, zeolite, cement kiln dust, lime, an elastomer, a resin, and any combination thereof.
  • 19. The method of claim 14 wherein the well bore has a bottom hole circulating temperature of about 40° F. to about 180° F.
  • 20. A method of cementing in a subterranean formation: providing a hydraulic cement,providing sub-micron alumina particles,preparing a cement composition, wherein the cement composition comprises: hydraulic cement;sub-micron alumina particles having a particle size in a range of about 150 nm to about 950 nm, wherein the sub-micron alumina particles are present in the cement composition in an amount in a range of about 0.1% to about 10% by weight of the hydraulic cement on a dry basis; andwater;introducing the cement composition into a subterranean formation; andallowing the cement composition to set in the subterranean formation.
  • 21. The method of claim 20 wherein the hydraulic cement comprises at least one hydraulic cement selected from the group consisting of a Portland cement, a pozzolana cement, a gypsum cement, a high-alumina-content cement, a slag cement, a silica/lime cement, and any combination thereof.
  • 22. The method of claim 20 wherein the cement composition comprises belite in an amount from 0.1% to about 50% by weight of calcium silicates in the cement composition.
  • 23. The method of claim 20 wherein the cement composition comprises a colloidal alumina dispersion comprising the sub-micron alumina particles suspended in a base fluid.
  • 24. The method of claim 20 wherein the cement composition further comprises a latex.
  • 25. The method of claim 24 wherein the latex comprises at least one rubber material selected from the group an ethylene-propylene rubber, a styrene-butadiene rubber, a nitrile rubber, a nitrile butadiene rubber, a butyl rubber, a neoprene rubber, a polybutadiene rubber, an acrylonitrile-styrene-butadiene rubber, a polyisoprene rubber, and any combination thereof.
  • 26. The method of claim 20 wherein the cement composition further comprises at least one additive selected from the group consisting of a latex stabilizer, 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 filtration-control additive, a fluid loss control additive, a dispersant, a defoaming agent, a foaming agent, a thixotropic additive, and any combination thereof.
  • 27. The method of claim 20 wherein the cement composition further comprises at least one additive selected from the group consisting of a gas, crystalline silica, amorphous silica, fumed silica, a salt, a fiber, a hydratable clay, calcined shale, vitrified shale, a microsphere, fly ash, slag, diatomaceous earth, metakaolin, rice husk ash, a natural pozzolan, zeolite, cement kiln dust, lime, an elastomer, a resin, and any combination thereof.
  • 28. The method of claim 20 wherein introducing the cement composition into the subterranean formation comprising introducing the cement composition into a well bore in a space between the subterranean formation and a conduit disposed in the well bore.
  • 29. The method of claim 28 wherein the well bore has a bottom hole circulating temperature of about 40° F. to about 180° F.
CROSS-REFERENCE TO RELATED APPLICATIONS

The present application is a continuation-in-part 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. 11/747,002, now U.S. Pat. No. 7,559,369, filed on May 10, 2007, entitled “Well Treatment Compositions and Methods Utilizing Nano-Particles.” The entire disclosures of these applications are incorporated herein by reference.

US Referenced Citations (418)
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
2857286 Striker Oct 1958 A
2871133 Palonen et al. Jan 1959 A
2880096 Hurley Mar 1959 A
2890169 Prokop Jun 1959 A
2933135 Johnson Apr 1960 A
2945769 Gama et al. Jul 1960 A
2952318 Ritch Sep 1960 A
2959223 Harmon et al. Nov 1960 A
2978024 Davis Apr 1961 A
3026938 Huitt et al. Mar 1962 A
3168139 Kennedy et al. Feb 1965 A
3219112 Sauber et al. Nov 1965 A
3336979 Ingraham et al. Aug 1967 A
3353601 Dollarhide et al. Nov 1967 A
3366177 Powers et al. Jan 1968 A
3381748 Peters et al. May 1968 A
3454095 Messenger et al. Jul 1969 A
3467193 Messenger Sep 1969 A
3499491 Wyant et al. Mar 1970 A
3557876 Tragesser Jan 1971 A
3607326 Serafin Sep 1971 A
RE27271 Hamsberger et al. Jan 1972 E
3748159 George Jul 1973 A
3854985 Suzuki et al. Dec 1974 A
3876005 Fincher et al. Apr 1975 A
3887009 Miller et al. Jun 1975 A
3887385 Quist et al. Jun 1975 A
3888311 Cooke, Jr. Jun 1975 A
3958638 Johnston May 1976 A
4018617 Nicholson Apr 1977 A
4031184 McCord Jun 1977 A
4036301 Powers et al. Jul 1977 A
4142910 Kraemer et al. Mar 1979 A
4176720 Wilson Dec 1979 A
4202795 Burnham et al. May 1980 A
4268316 Wills, Jr. May 1981 A
4274881 Langton et al. Jun 1981 A
4284433 Aignesberger et al. Aug 1981 A
4341562 Ahlbeck Jul 1982 A
RE31190 Detroit et al. Mar 1983 E
4407677 Wills, Jr. 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
4506734 Nolte Mar 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
4643362 Serafin Feb 1987 A
4650520 Johnsen et al. Mar 1987 A
4660642 Young Apr 1987 A
4676317 Fry et al. Jun 1987 A
4676832 Childs et al. Jun 1987 A
4700777 Luers Oct 1987 A
4711401 Serafin Dec 1987 A
4721160 Parcevaux et al. Jan 1988 A
4741401 Walles et al. May 1988 A
4741782 Styron May 1988 A
4770796 Jacobs Sep 1988 A
4784223 Worrall et al. Nov 1988 A
4848973 Yokota et al. Jul 1989 A
4883125 Wilson et al. Nov 1989 A
4941536 Brothers et al. Jul 1990 A
4953620 Bloys et al. Sep 1990 A
4961790 Smith et al. Oct 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
5102558 McDougall et al. Apr 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
5151203 Riley et al. Sep 1992 A
5183505 Spinney Feb 1993 A
5203629 Valle et al. Apr 1993 A
5207832 Baffreau et al. May 1993 A
5213160 Nahm et al. May 1993 A
5236501 Nomachi et al. Aug 1993 A
5238064 Dahl et al. Aug 1993 A
5253991 Yokota et al. Oct 1993 A
5263542 Brothers Nov 1993 A
5266111 Barbour Nov 1993 A
5292512 Schaefer et al. Mar 1994 A
5295543 Terry et al. Mar 1994 A
5305831 Nahm Apr 1994 A
5314022 Cowan et al. May 1994 A
5320851 Mars et al. Jun 1994 A
5327968 Onan et al. Jul 1994 A
5337824 Cowan Aug 1994 A
5339903 Eoff et al. Aug 1994 A
5340397 Brothers Aug 1994 A
5346012 Heathman et al. Sep 1994 A
5352288 Mallow Oct 1994 A
5358044 Hale et al. Oct 1994 A
5358047 Himes 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
5373901 Norman et al. Dec 1994 A
5375661 Daneshy et al. Dec 1994 A
5382290 Nahm et al. Jan 1995 A
5383521 Onan et al. Jan 1995 A
5383967 Chase Jan 1995 A
5389706 Heathman et al. Feb 1995 A
5398758 Onan et al. Mar 1995 A
5398759 Rodrigues et al. Mar 1995 A
5423379 Hale et al. Jun 1995 A
5439056 Cowan Aug 1995 A
5454867 Brothers et al. Oct 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
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
5551976 Allen Sep 1996 A
5569324 Totten et al. Oct 1996 A
5575841 Dry Nov 1996 A
5580379 Cowan Dec 1996 A
5585333 Dahl et al. Dec 1996 A
5588488 Vijn et al. Dec 1996 A
5588489 Chatterji et al. Dec 1996 A
5603961 Suzuki et al. Feb 1997 A
5660624 Dry Aug 1997 A
5663230 Haman Sep 1997 A
5673753 Hale et al. Oct 1997 A
5688844 Chatterji et al. Nov 1997 A
5711383 Terry et al. Jan 1998 A
5716910 Totten et al. Feb 1998 A
5728209 Bury et al. Mar 1998 A
5728654 Dobson et al. Mar 1998 A
5741357 Sheikh Apr 1998 A
5766323 Butler et al. Jun 1998 A
5779787 Brothers et al. Jul 1998 A
5783541 Tack et al. Jul 1998 A
5795060 Stephens Aug 1998 A
5820670 Chatterji et al. Oct 1998 A
5851960 Totten et al. Dec 1998 A
5866516 Costin Feb 1999 A
5874387 Carpenter et al. Feb 1999 A
5879699 Lerner Mar 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
5989334 Dry Nov 1999 A
6022408 Stokes et al. Feb 2000 A
6027561 Gruber 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
6180689 Moulin 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
6261360 Dry 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
6390197 Maroy May 2002 B1
6402833 O'Hearn et al. Jun 2002 B1
6409819 Ko Jun 2002 B1
6444316 Reddy et al. Sep 2002 B1
6457524 Roddy Oct 2002 B1
6471975 Banovetz et al. Oct 2002 B1
6478869 Reddy et al. Nov 2002 B2
6488089 Bour et al. Dec 2002 B1
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
6500253 Norman et al. Dec 2002 B2
6502636 Chatterji et al. Jan 2003 B2
6508305 Brannon et al. Jan 2003 B1
6524384 Griffith et al. Feb 2003 B2
6527051 Reddy et al. Mar 2003 B1
6527849 Dry Mar 2003 B2
6547871 Chatterji et al. Apr 2003 B2
6547891 Linden et al. Apr 2003 B2
6554067 Davies et al. Apr 2003 B1
6554071 Reddy et al. Apr 2003 B1
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
6599863 Palmer et al. Jul 2003 B1
6610139 Crook et al. Aug 2003 B2
6626243 Go Boncan Sep 2003 B1
6631766 Brothers et al. Oct 2003 B2
6632527 McDaniel et al. Oct 2003 B1
6645288 Dargaud et al. Nov 2003 B1
6645290 Barbour Nov 2003 B1
6648962 Berke et al. Nov 2003 B2
6656265 Garnier et al. Dec 2003 B1
6656266 Barlet-Gouedard 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
6808561 Genge Oct 2004 B2
6811603 Brothers et al. Nov 2004 B2
6823940 Reddy et al. Nov 2004 B2
6832651 Ravi et al. Dec 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
6861392 Shaarpour Mar 2005 B2
6874578 Garnier et al. Apr 2005 B1
6883609 Drochon et al. Apr 2005 B2
6887833 Brothers et al. May 2005 B2
6889767 Reddy et al. May 2005 B2
6902001 Dargaud et al. Jun 2005 B2
6904971 Brothers et al. Jun 2005 B2
6907929 Leroy-Delage et al. Jun 2005 B2
6908508 Brothers Jun 2005 B2
6911078 Barlet-Gouedard et al. Jun 2005 B2
6926081 Sweatman et al. Aug 2005 B2
6962201 Brothers Nov 2005 B2
7007755 Reddy et al. Mar 2006 B2
7022179 Dry Apr 2006 B1
7026272 Reddy et al. Apr 2006 B2
7032664 Lord et al. Apr 2006 B2
7033975 Baran et al. Apr 2006 B2
7048053 Santra et al. May 2006 B2
7059415 Bosma et al. Jun 2006 B2
7077203 Roddy et al. Jul 2006 B1
7084092 Patel et al. Aug 2006 B2
7086466 Roddy Aug 2006 B2
7138446 Reddy et al. Nov 2006 B2
7143828 Reddy et al. Dec 2006 B2
7143832 Freyer Dec 2006 B2
7156173 Mueller Jan 2007 B2
7156174 Roddy et al. Jan 2007 B2
7172022 Reddy et al. Feb 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
7204312 Roddy et al. Apr 2007 B2
7213646 Roddy et al. May 2007 B2
7264053 Vargo, Jr. et al. Sep 2007 B2
7279447 Lal et al. Oct 2007 B2
7284609 Roddy et al. Oct 2007 B2
7284611 Reddy et al. Oct 2007 B2
7294194 Reddy et al. Nov 2007 B2
7296597 Freyer et al. Nov 2007 B1
7303014 Reddy et al. Dec 2007 B2
7335252 Roddy et al. Feb 2008 B2
7337841 Ravi Mar 2008 B2
7337842 Roddy et al. Mar 2008 B2
7338923 Roddy et al. Mar 2008 B2
7341104 Roddy et al. Mar 2008 B2
7351279 Brothers 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
7404440 Reddy et al. Jul 2008 B2
7409991 Reddy et al. Aug 2008 B2
7422060 Hammami et al. Sep 2008 B2
7424913 Roddy Sep 2008 B2
7445668 Sommain Nov 2008 B2
7445669 Roddy et al. Nov 2008 B2
7451817 Reddy et al. Nov 2008 B2
7461696 Nguyen et al. Dec 2008 B2
7478675 Roddy et al. Jan 2009 B2
7478678 Farrar et al. Jan 2009 B2
7482309 Ravi et al. Jan 2009 B2
7559369 Roddy et al. Jul 2009 B2
7784542 Roddy et al. Aug 2010 B2
7806183 Roddy et al. Oct 2010 B2
7846876 Koyanagi Dec 2010 B2
7892352 Roddy et al. Feb 2011 B2
1305247 Ravi et al. Mar 2011 A1
8114820 Crews Feb 2012 B2
8226879 Genolet et al. Jul 2012 B2
20020004464 Nelson et al. Jan 2002 A1
20020033121 Marko Mar 2002 A1
20020073894 Genge et al. Jun 2002 A1
20020073897 Trato Jun 2002 A1
20020117090 Ku Aug 2002 A1
20020193257 Lee et al. Dec 2002 A1
20030089281 Berke et al. May 2003 A1
20030116065 Griffith et al. Jun 2003 A1
20030116887 Scott Jun 2003 A1
20030134751 Lee et al. Jul 2003 A1
20030167970 Polston Sep 2003 A1
20030168215 Drochon et al. Sep 2003 A1
20030220204 Baran et al. Nov 2003 A1
20030234103 Lee et al. Dec 2003 A1
20040007162 Morioka et al. Jan 2004 A1
20040040475 De La Roij et al. Mar 2004 A1
20040055748 Reddy 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
20040144537 Reddy et al. Jul 2004 A1
20040171499 Ravi et al. Sep 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
20040261990 Bosma et al. Dec 2004 A1
20040261999 Nguyen Dec 2004 A1
20050000734 Getzlaf et al. Jan 2005 A1
20050022991 Rao Feb 2005 A1
20050034867 Griffith et al. Feb 2005 A1
20050056191 Brothers et al. Mar 2005 A1
20050061206 Reddy et al. Mar 2005 A1
20050072599 Luke et al. Apr 2005 A1
20050084334 Shi et al. Apr 2005 A1
20050096207 Urbanek May 2005 A1
20050098317 Reddy et al. May 2005 A1
20050113260 Wood May 2005 A1
20050113262 Ravi et al. May 2005 A1
20050133221 Chatterji et al. Jun 2005 A1
20050173117 Roddy Aug 2005 A1
20050199401 Patel et al. Sep 2005 A1
20060016598 Urbanek Jan 2006 A1
20060025312 Santra et al. Feb 2006 A1
20060086503 Reddy et al. Apr 2006 A1
20060089851 Silby et al. Apr 2006 A1
20060122071 Reddy et al. Jun 2006 A1
20060162926 Roddy Jul 2006 A1
20060166834 Roddy Jul 2006 A1
20060177661 Smith et al. Aug 2006 A1
20060260512 Nordmeyer Nov 2006 A1
20060260513 Guiterrez et al. Nov 2006 A1
20060278131 Hunt Dec 2006 A1
20070012436 Freyer Jan 2007 A1
20070015668 Harrower et al. Jan 2007 A1
20070017676 Reddy et al. Jan 2007 A1
20070056475 Roddy et al. Mar 2007 A1
20070056479 Gray Mar 2007 A1
20070056732 Roddy et al. Mar 2007 A1
20070056733 Roddy et al. Mar 2007 A1
20070062691 Reddy et al. Mar 2007 A1
20070102157 Roddy et al. May 2007 A1
20070125534 Reddy et al. Jun 2007 A1
20070137528 LeRoy-Delage et al. Jun 2007 A1
20070151484 Reddy et al. Jul 2007 A1
20070151724 Ohmer et al. Jul 2007 A1
20070151730 Reddy et al. Jul 2007 A1
20070186820 O'Hearn Aug 2007 A1
20070204765 LeRoy-Delage et al. Sep 2007 A1
20070227734 Freyer Oct 2007 A1
20070246225 Hailey, Jr. et al. Oct 2007 A1
20070255457 Whitcomb et al. Nov 2007 A1
20080017376 Badalamenti et al. Jan 2008 A1
20080058229 Berkland et al. Mar 2008 A1
20080099203 Mueller et al. May 2008 A1
20080108524 Willberg et al. May 2008 A1
20080135250 Bosma et al. Jun 2008 A1
20080156491 Roddy et al. Jul 2008 A1
20080261027 Li et al. Oct 2008 A1
20080261834 Simon Oct 2008 A1
20080261934 Simon Oct 2008 A1
20080277116 Roddy et al. Nov 2008 A1
20090088348 Roddy Apr 2009 A1
20090114126 Roddy May 2009 A1
20090120644 Roddy May 2009 A1
20090124522 Roddy May 2009 A1
20090139719 Luo Jun 2009 A1
20090200029 Roddy et al. Aug 2009 A1
20090236097 Roddy et al. Sep 2009 A1
20090260544 Roddy Oct 2009 A1
20100016183 Roddy et al. Jan 2010 A1
20100025039 Roddy et al. Feb 2010 A1
20100075874 Mercado et al. Mar 2010 A1
20100096135 Roddy et al. Apr 2010 A1
20110162845 Ravi et al. Jul 2011 A1
Foreign Referenced Citations (40)
Number Date Country
2153372 Jan 2006 CA
101544488 Sep 2009 CN
102007042078 Mar 2009 DE
0748782 Dec 1996 EP
0814067 Dec 1997 EP
1236701 Sep 2002 EP
1394137 Jul 2003 EP
1348831 Oct 2003 EP
1686234 Aug 2006 EP
1719741 Nov 2006 EP
2465910 Nov 2009 EP
2787105 Jun 2000 FR
1469954 Apr 1997 GB
2429725 Mar 2007 GB
52117316 Oct 1977 JP
10110487 Apr 1998 JP
1373781 Feb 1988 SU
WO 8301443 Apr 1983 WO
9011977 Oct 1990 WO
WO 9705079 Feb 1997 WO
WO 9749644 Dec 1997 WO
WO 9854108 Dec 1998 WO
WO 0063134 Jan 2000 WO
WO 0049272 Aug 2000 WO
WO 0050357 Aug 2000 WO
WO 0187796 Nov 2001 WO
WO 03008756 Jan 2003 WO
WO 03031364 Apr 2003 WO
WO 2004001188 Dec 2003 WO
WO 2004057715 Jul 2004 WO
WO 2004101951 Nov 2004 WO
WO 2004101952 Nov 2004 WO
WO 2005047212 May 2005 WO
WO 2005061846 Jul 2005 WO
WO 2005080287 Aug 2005 WO
WO 2006032841 Mar 2006 WO
WO 2006053896 May 2006 WO
2008034461 Mar 2008 WO
WO 2008034461 Mar 2008 WO
WO 2009030758 Mar 2009 WO
Non-Patent Literature Citations (201)
Entry
“Effect of the particle size on the micro and nanostructural features of calcium phosphate cement: a kinetic analysis”, Biomaterials 25 (2004) 3453-3462.
USPTO Notice of Allowance from U.S. Appl. No. 12/426,393, dated Dec. 16, 2010.
“Effect of Nano-SiO2 on heat of hydration of portland cement,” Xu et al., Nanjing Gongye Daxue Xuebao, Ziran Kexeuban (2007), 29(4), 45-48, abstract only.
“Application of nanometer silica in inorganic nonmetallic materials,” Deng et al., Taoci (Xiangyang China) 2007, (9), 8-12, abstract only.
“Reaction mechanism analyses of cement based composite materials modified by nano-silica,” Xu et al., Kuangye Gongcheng (Changsha, China), 2007, 27(3), 99-102, abstract only.
“Research on Reinforcement of cement composites and relevant mechanism,” Yu et al., Qiangdoa Keji Daxue Xuebao, Ziran Kexueban (2006), 27(2), 148-151, abstract only.
“Antagonistic Effect of superplasticizer and colloidal nanosilica in the hydration of Alite and Belite pastes,” Bjoernstrom et al., Journal of Materials Science, 2007, 42(11), 3901-3907, abstract only.
“Nano-concrete: possibilities and challenges,” Balaguru et al., RILEM Proceedings (2005), PRO 45 (2nd Int'l Symposium on Nanotechnology in construction (NICOM2), 2005, 233-243, abstract only.
“A comparative study on the pozzolanic activity between nano-SiO2 and silica fume,” Ye et al., Journal of Wuhan Univ of Technology, Mat'ls Science Edition (2006), 21(3), 153-157, abstract only.
“Optimization of silica fume, fly ash and amorphous nano-silica in superplasticized high-performance concrete,” Collepardi et al., American Concrete Institute, SP 2004, SP-221 (Eight CANMET/ACI International Conference on Fly Ash, Silica Fume, Slag, and Natrural Pozzolans in Concrete, 2004), 495-505, abstract only.
“Accelerating effects of colloidal nano-silica for beneficial calcium-silicate-hydrate formation in cement,” Bjornstrom et al., Chemical Physics Letters (2004), 392 (1-3), 242-248, abstract only.
“Experimental study on cement-based composites with nano-SiO2,” Feng et al., Cailiao Kexue Yu Gongcheng Zuebao Bianjibu (2004), 22(2), 224-227.
“Strong and bioactive composites containing nano-silica-fused whiskers for bone repair,” Xu et al., Biomaterials (2004), 25(19), 4615-4626, abstract only.
Research on properties of Portland cement added with nano-SiO2, Wang et al., RILEM Proceedings (2003), PRO 32 (International Conference on Advances in Concrete and Structures, 2003, vol. 1), 154-161, abstract only.
“Comparison on properties of high strength concrete with nano-SiO2 and silica fume added,” Ye et al., Jianzhu Cailiao Xuebao (2003), 6(4), 381-385, abstract only.
“Study on compound effect of silica fume and nano-SiOx for cementing composite materials,” Tang et al., Guisuanyan Xuebao (2003), 3(5), 523-527, abstract only.
“Effect of nano-SiOx and silica fume on cement paste water demand,” Li et al., Shenyang Jianzhu gongcheng Xueyuan Xuebao, Ziran Kexueban (2002), 18(4), 278-281, abstract only.
“Hydration reaction between C3S and fly ash, silica fume, nano-SiO2, and microstructure of hydrated pastes,” Ba et al., Guisuanyan Xuebao (2002), 30(6), 780-784, abstract only.
“Nano-silica—an additive for high-strength concrete,” Wagner et al., Wissenschaftliche Zeitschrift—Hoschule fuer Architektur und Bauwesen Weimar—Universitaet (1994), 40 (5/6/7), 183-87, abstract only.
“Investigations on the preparation and mechanical properties of the nano-alumina reinforced cement composite,” Li et al., Materials Letters (2006), 0(3), 356-359, abstract only.
“Effect of secondary interface microstructure on pore structure and performance of cement-based materials,” Feng et al., Cailiao Yanjiu Xuebao (2003), 17(5), 489-494, abstract only.
“Preparation of multifunctional dry-power paints,” Yanmin Gao, Faming Zhuanli Shenqing gongkai Shuomingshu, 4 pages, 2005, abstract only.
USPTO office action from U.S. Appl. No. 12/426,393, dated Jul. 2, 2010.
USPTO notice of allowance from U.S. Appl. No. 12/472,561, dated Jun. 29, 2010.
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 (undated but admitted as prior art).
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” (undated but admitted as prior art).
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) (undated but admitted as prior art).
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, 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. 11/416,754 (Notice of Allowance), Jul. 2, 2007.
Office Action from U.S. Appl. No. 11/223,485 (Notice of Allowance), Aug. 3, 2007.
Office Action from U.S. Appl. No. 11/257,261, Aug. 10, 2007.
Office Action from U.S. Appl. No. 11/271,690 (Notice of Allowance), Aug. 13, 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. 11/416,754 (Notice of Allowance), Oct. 17, 2007.
Office Action from U.S. Appl. No. 11/257,261 (Notice of Allowance), Oct. 23, 2007.
Office Action from U.S. Appl. No. 11/402,741, Oct. 24, 2007.
Office Action from U.S. Appl. No. 11/223,750 (Notice of Allowance), Dec. 11, 2007.
Office Action from U.S. Appl. No. 11/402,741 (Notice of Allowance), Dec. 13, 2007.
Office Action from U.S. Appl. No. 11/223,669, Jan. 29, 2008.
Office Action from U.S. Appl. No. 11/256,824 (Notice of Allowance), Feb. 27, 2008.
Office Action from U.S. Appl. No. 11/223,703 (Notice of Allowance), Feb. 27, 2008.
Office Action from U.S. Appl. No. 11/223,669, Apr. 8, 2008.
Office Action from U.S. Appl. No. 11/223,669 (Notice of Allowance), Jun. 30, 2008.
Foreign Search Report from a Related Application, Sep. 9, 2005.
Foreign Search Report from a Related Application, Jul. 5, 2006.
Foreign Search Report from a Related Application, Oct. 27, 2006.
Foreign Search Report from a Related Application, Nov. 2, 2006.
Foreign Search Report from a Related Application, Dec. 1, 2006.
Foreign Search Report from a Related Application, Dec. 19, 2006.
Foreign Search Report from a Related Application, May 8, 2007.
Office Action from U.S. Appl. No. 12/034,886 (Notice of Allowance), 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. Material Science, May 18, 2007.
Foreign communication from a related counterpart application, Jul. 5, 2005.
Office Action from U.S. Appl. No. 10/775,348, Nov. 23, 2005.
Office Action from U.S. Appl. No. 10/775,348, May 2, 2006.
Notice of Allowance from U.S. Appl. No. 10/775,348, Jun. 6, 2006.
Foreign communication from a related counterpart application, Jun. 29, 2007.
Notice of Allowance from U.S. Appl. No. 11/388,644, Jan. 3, 2008.
Office Action from U.S. Appl. No. 12/008,923, May 20, 2008.
Notice of Allowance from U.S. Appl. No. 12/008,923, Jul. 22, 2008.
Office Action from U.S. Appl. No. 11/388,645, Apr. 3, 2009.
Office Action from U.S. Appl. No. 11/388,645, Jul. 30, 2009.
Nanocor Technical brochure entitled “Nanoclay Structures”, Mar. 18, 2009.
Nanofil SE 3000, “Active nanofiller for polymr applications”, Product Bulletin/Nanofil, Southern Clay Products.
Halliburton brochure entitled, “Cementing WellLife III Cementing Service”, Apr. 2008.
Darbe, “Slurry Design Considerations for Mechanically Enhanced Cement Systems”, AADE-08-DF-HO-06, 2008.
Halamickova, “Water Permeability and Chloride Ion Diffusion in Portland Cement Mortars: Relationship to Sand Content and Critical Pore Diameter”, Cement and Concrete Research, vol. 25, No. 4, pp. 790-802, 1995.
Montmorillonite, Wikipedia encyclopedia, 2009.
Ravi, “Interventionless Zonal Isolation”, Cementing, May 2008.
Schlumberger brochure, “Futur Active set-cement technology for long-term zonal isolation”, 2007.
Halliburton brochure, “WellLife III Cementing Service for CO2 Environments”, Jun. 2009.
Hunter, “Three Key Mechanisms Deliver Zonal Isolation”, IADC.
Office Action from U.S. Appl. No. 11/747,002, Apr. 2, 2008.
Office Action from U.S. Appl. No. 11/747,002, May 27, 2008.
Office Action from U.S. Appl. No. 11/747,002, Jul. 10, 2008.
Office Action from U.S. Appl. No. 11/747,002, Mar. 3, 2009.
PCT International Search Report and Written Opinion for International Application No. PCT/GB2010/000485 dated May 21, 2010.
PCT International Search Report for International Application No. PCT/GB2010/001806, dated Jan. 20, 2011.
PCT Written Opinion for International Application No. PCT/GB2010/001806, dated Jan. 20, 2011.
English language abstract of CN 101544488, published Sep. 30, 2009.
Office Action from U.S. Appl. No. 12/426,645, dated May 5, 2010.
Office Action from U.S. Appl. No. 12/472,561, dated May 5, 2010.
USPTO Office Action for U.S. Appl. No. 12/833,189 dated Feb. 17, 2011.
International Search Report for PCT/GB/2010/001045 dated Jul. 21, 2010.
Written Opinion of the International Searching Authority for PCT/GB/2010/001045 dated Jul. 21, 2010.
USPTO Office Action for U.S. Appl. No. 11/388,645 dated Aug. 17, 2010.
PCT International Searching Authority for International Application No. PCT/GB2009/002596 dated Feb. 8, 2010.
USPTO Office Action for U.S. Appl. No. 12/833,189 dated Oct. 1, 2010.
USPTO Office Action for U.S. Appl. No. 12/833,189 dated Nov. 10, 2010.
USPTO Office Action for U.S. Appl. No. 12/567,782 dated Apr. 5, 2011.
USPTO Office Action for U.S. Appl. No. 12/567,783 dated Apr. 6, 2011.
MacLaren et al., “Cement: Its Chemistry and Properties”, Chemistry for Everyone, vol. 80, No. 6, Journal of Chemical Education, pp. 623-635, Jun. 2003.
Hewlett, Peter C., “Lea's Chemistry of Cement and Concrete”, Fourth Edition, Elsevier Ltd., pp. 716-722, 1998.
“Calcium aluminate cements”, Retrieved from “http://en.wikipedia.org/wiki/Calcium—aluminate—cements”, pp. 1-3, Feb. 2011.
“Calcium aluminates”, Retrieved from “http://en.wikipedia.org/wiki/Calcium—aluminates”, pp. 1-2, Mar. 2011.
USPTO Office Action for U.S. Appl. No. 12/263,954 dated Aug. 8, 2011.
USPTO Office Action for U.S. Appl. No. 12/567,783 dated Aug. 23, 2011.
USPTO Office Action for U.S. Appl. No. 12/833,189 dated Oct. 11, 2011.
Campillo et al., “Improvement of initial mechanical strength by nanoalumina in belite cements”, Science Direct, Materials Letters 61, pp. 1889-1892, 2007.
PCT International Search Report and Written Opinion for International Application No. PCT/GB2011/000003 dated Apr. 18, 2011.
USPTO Office Action for U.S. Appl. No. 12/833,189 dated Jul. 18, 2011.
USPTO Office Action for U.S. Appl. No. 12/263,954 dated Apr. 20, 2011.
USPTO Office Action for U.S. Appl. No. 12/567,782 dated Apr. 25, 2011.
USPTO Office Action for U.S. Appl. No. 12/833,189 dated May 16, 2011.
USPTO Office Action for U.S. Appl. No. 12/833,189 dated Feb. 7, 2012.
HES Brochure “Latex 2000”, Aug. 2006.
USPTO Office Action for U.S. Appl. No. 12/567,782 dated Mar. 2, 2012.
USPTO Office Action for U.S. Appl. No. 13/052,471 dated Mar. 6, 2012.
International Search Report for PCT/GB2010/001805 dated Mar. 31, 2011.
Written Opinion for PCT/GB2010/001805 dated Mar. 27, 2012.
USPTO Office Action for U.S. Appl. No. 13/431,701 dated Nov. 9, 2012.
USPTO Office Action for U.S. Appl. No. 12/567,782 dated Jul. 25, 2012.
USPTO Office Action for U.S. Appl. No. 13/052,471 dated Jun. 28, 2012.
Written Opinion of the International Searching Authority for PCT/GB/2010/000485 dated Oct. 25, 2011.
Written Opinion of the International Searching Authority for PCT/GB/2011/000003 dated Jul. 12, 2012.
Communication from EPO for EPO App. No. 12159772.8 dated May 3, 2012.
Li et al., “Investigations on the preparation and mechanical properties of the nano-alumina reinforced cement composite”, Science Direct, Materials Letters 60, pp. 356-359, 2006.
Office Action from U.S. Appl. No. 12/567,782 dated Feb. 8, 2013.
Office Action from U.S. Appl. No. 13/435,701 dated Feb. 19, 2013.
Office Action from U.S. Appl. No. 13/458,112 dated Mar. 15, 2013.
Office Action from U.S. Appl. No. 12/833,189 dated Feb. 6, 2013.
Office Action from U.S. Appl. No. 13/443,934 dated Mar. 4, 2013.
International Search Report and Written Opinion for PCT/GB2010/0010445 dated Jul. 21, 2010.
Office Action from U.S. Appl. No. 13/052,471 dated Feb. 4, 2013.
Office Action from U.S. Appl. No. 12/263,954 dated Mar. 14, 2013.
Related Publications (1)
Number Date Country
20100095871 A1 Apr 2010 US
Continuation in Parts (2)
Number Date Country
Parent 12263954 Nov 2008 US
Child 12651662 US
Parent 11747002 May 2007 US
Child 12263954 US