WO2011078985A1 - A proppant having a glass-ceramic material - Google Patents

A proppant having a glass-ceramic material Download PDF

Info

Publication number
WO2011078985A1
WO2011078985A1 PCT/US2010/060029 US2010060029W WO2011078985A1 WO 2011078985 A1 WO2011078985 A1 WO 2011078985A1 US 2010060029 W US2010060029 W US 2010060029W WO 2011078985 A1 WO2011078985 A1 WO 2011078985A1
Authority
WO
WIPO (PCT)
Prior art keywords
proppant
glass
ceramic
sphere
oxide
Prior art date
Application number
PCT/US2010/060029
Other languages
English (en)
French (fr)
Inventor
Yuming Xie
Dilip Chatterjee
Christopher E. Coker
Christopher Y. Fang
Original Assignee
Oxane Materials, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Oxane Materials, Inc. filed Critical Oxane Materials, Inc.
Priority to EP10839988.2A priority Critical patent/EP2516152A4/en
Priority to CN201080064478.0A priority patent/CN102781663B/zh
Priority to IN5062DEN2012 priority patent/IN2012DN05062A/en
Priority to CA2785366A priority patent/CA2785366C/en
Priority to MX2012007248A priority patent/MX2012007248A/es
Priority to AU2010333894A priority patent/AU2010333894B2/en
Priority to BR112012015322A priority patent/BR112012015322A2/pt
Priority to EA201290543A priority patent/EA201290543A1/ru
Publication of WO2011078985A1 publication Critical patent/WO2011078985A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/60Compositions for stimulating production by acting on the underground formation
    • C09K8/80Compositions for reinforcing fractures, e.g. compositions of proppants used to keep the fractures open
    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/25Methods for stimulating production
    • E21B43/26Methods for stimulating production by forming crevices or fractures
    • E21B43/267Methods for stimulating production by forming crevices or fractures reinforcing fractures by propping
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B17/00Layered products essentially comprising sheet glass, or glass, slag, or like fibres
    • B32B17/02Layered products essentially comprising sheet glass, or glass, slag, or like fibres in the form of fibres or filaments
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C10/00Devitrified glass ceramics, i.e. glass ceramics having a crystalline phase dispersed in a glassy phase and constituting at least 50% by weight of the total composition
    • C03C10/0036Devitrified glass ceramics, i.e. glass ceramics having a crystalline phase dispersed in a glassy phase and constituting at least 50% by weight of the total composition containing SiO2, Al2O3 and a divalent metal oxide as main constituents
    • C03C10/0045Devitrified glass ceramics, i.e. glass ceramics having a crystalline phase dispersed in a glassy phase and constituting at least 50% by weight of the total composition containing SiO2, Al2O3 and a divalent metal oxide as main constituents containing SiO2, Al2O3 and MgO as main constituents
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C11/00Multi-cellular glass ; Porous or hollow glass or glass particles
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/626Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
    • C04B35/62605Treating the starting powders individually or as mixtures
    • C04B35/62695Granulation or pelletising
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/626Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
    • C04B35/628Coating the powders or the macroscopic reinforcing agents
    • C04B35/62802Powder coating materials
    • C04B35/62805Oxide ceramics
    • C04B35/62807Silica or silicates
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/60Compositions for stimulating production by acting on the underground formation
    • C09K8/80Compositions for reinforcing fractures, e.g. compositions of proppants used to keep the fractures open
    • C09K8/805Coated proppants
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2235/00Aspects relating to ceramic starting mixtures or sintered ceramic products
    • C04B2235/02Composition of constituents of the starting material or of secondary phases of the final product
    • C04B2235/30Constituents and secondary phases not being of a fibrous nature
    • C04B2235/32Metal oxides, mixed metal oxides, or oxide-forming salts thereof, e.g. carbonates, nitrates, (oxy)hydroxides, chlorides
    • C04B2235/3231Refractory metal oxides, their mixed metal oxides, or oxide-forming salts thereof
    • C04B2235/3232Titanium oxides or titanates, e.g. rutile or anatase
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2235/00Aspects relating to ceramic starting mixtures or sintered ceramic products
    • C04B2235/02Composition of constituents of the starting material or of secondary phases of the final product
    • C04B2235/30Constituents and secondary phases not being of a fibrous nature
    • C04B2235/34Non-metal oxides, non-metal mixed oxides, or salts thereof that form the non-metal oxides upon heating, e.g. carbonates, nitrates, (oxy)hydroxides, chlorides
    • C04B2235/3427Silicates other than clay, e.g. water glass
    • C04B2235/3463Alumino-silicates other than clay, e.g. mullite
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2235/00Aspects relating to ceramic starting mixtures or sintered ceramic products
    • C04B2235/02Composition of constituents of the starting material or of secondary phases of the final product
    • C04B2235/50Constituents or additives of the starting mixture chosen for their shape or used because of their shape or their physical appearance
    • C04B2235/52Constituents or additives characterised by their shapes
    • C04B2235/528Spheres
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2235/00Aspects relating to ceramic starting mixtures or sintered ceramic products
    • C04B2235/02Composition of constituents of the starting material or of secondary phases of the final product
    • C04B2235/50Constituents or additives of the starting mixture chosen for their shape or used because of their shape or their physical appearance
    • C04B2235/54Particle size related information
    • C04B2235/5418Particle size related information expressed by the size of the particles or aggregates thereof
    • C04B2235/5436Particle size related information expressed by the size of the particles or aggregates thereof micrometer sized, i.e. from 1 to 100 micron
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S507/00Earth boring, well treating, and oil field chemistry
    • Y10S507/904Process of making fluids or additives therefor
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S507/00Earth boring, well treating, and oil field chemistry
    • Y10S507/906Solid inorganic additive in defined physical form

Definitions

  • the present invention relates to proppants and methods to make the proppants and uses of the proppants.
  • the proppant or a portion thereof has a glass- ceramic material present.
  • the presence of a glass-ceramic material can provide one or more benefits, such as increased stiffness (or modulus of rigidity, "MOR"), a desirable coefficient of thermal expansion, and/or other benefits.
  • MOR modulus of rigidity
  • Proppants are materials pumped into oil or gas wells at extreme pressure in a carrier solution (typically brine) during the hydrofracturing process. Once the pumping-induced pressure is removed, proppants "prop" open fractures in the rock formation and thus preclude the fracture from closing. As a result, the amount of formation surface area exposed to the well bore is increased, enhancing recovery rates.
  • a carrier solution typically brine
  • Ceramic proppants are widely used as propping agents to maintain permeability in oil and gas formations.
  • High strength ceramic proppants have been used in the hydrofracture of subterranean earth in order to improve production of natural gas and/or oil.
  • the proppant beads need to withstand 10 kpsi or higher pressure to be effective to prop the fracture generated by the hydrofracture process.
  • proppants formed from high strength materials such as sintered bauxite and alumina have sufficient compressive and flexural strength for use in deep wells.
  • These conventional high strength materials are expensive, however, because of a limited supply of raw materials, a high requirement for purity, and the complex nature of the manufacturing process.
  • a feature of the present invention is to provide a proppant having an improved coefficient of thermal expansion. Another feature of the present invention is to provide a proppant that can provide increased stiffness (modulus of rigidity).
  • An additional feature of the present invention is to provide a proppant having better resistance to fracturing.
  • a further feature of the present invention is to provide a proppant that can have less discreet interfaces between various layers that can form the proppant.
  • the present invention relates to a proppant having a template sphere.
  • the proppant optionally has a shell that can be sintered around the entire outer surface of the template sphere.
  • the optional shell can comprise glass- ceramic.
  • the optional shell which can comprise one or more layers, can contain one or more metal oxides, a ceramic material or oxide thereof, and/or other suitable materials.
  • the outer surface of the template sphere can include or have a glass-ceramic material.
  • a glass-ceramic containing layer can be present on the outer surface of the template sphere.
  • the present invention further relates to a method to prop open subterranean formation fractions using one or more proppants of the present invention, which can be contained in proppant formulations.
  • the present invention further relates to methods of making the various proppants of the present invention.
  • one method includes crystallizing at least an outer surface of a template material to form glass-ceramic, and coating the template material with a formulation comprising a ceramic material or oxide thereof and/or one or more metal oxides and/or other material to form a shell around the template and then hardening the shell, such as by sintering or calcining.
  • Other methods are further described.
  • Figure 1 is a graph showing the density of the cenosphere powder-derived glass- ceramics of the present invention as a function of Ti0 2 content. All the samples were sintered at 1200°C for 4h.
  • Figure 2 is a graph showing the diametral splitting tensile strength of the cenosphere- derived glass-ceramics of the present invention as a function of Ti0 2 content. All the samples were sintered at 1200°C for 4h.
  • Figure 3 is a graph showing the specific diametral splitting tensile strength of the cenosphere-derived glass-ceramics of the present invention as a function of Ti0 2 content.
  • the present invention relates to a proppant, methods of making the proppant, and uses for the proppant, including using the proppant for assisting in hydrocarbon recovery.
  • the present invention relates to a proppant having present a glass-ceramic or a glass- ceramic material as part of the proppant.
  • the proppant comprises one or more components
  • one or more of the components can contain the glass-ceramic.
  • the proppant can be a template sphere or core, and at least the outer surface of the template sphere or core can be or can comprise or consist essentially of or consist of one or more glass-ceramics.
  • the proppant can be a template sphere having one or more layers located on the sphere. At least one of these layers can comprise, consist essentially of, or consist of one or more glass-ceramics.
  • a proppant can be a template sphere (which can optionally contain a glass-ceramic) that has a glass-ceramic containing layer in contact (direct contact or in contact with a layer located on said template sphere) with at least the outer surface of the template sphere.
  • the proppant can be a template sphere having an outer surface wherein the outer surface of the template sphere comprises a glass-ceramic(s) and further has at least one layer in contact (direct contact or in contact with a layer located on said template sphere) with the outer surface of the template sphere, wherein the layer(s) comprises a glass-ceramic(s).
  • the glass- ceramic containing layer can at least partially diffuse into the outer surface of the template sphere.
  • the template sphere (which also can be referred to as a core or substrate) can be a solid sphere or a hollow sphere, or a sphere having one or more voids or a sphere having porosity. It should be understood that a solid sphere, as used herein, does not contain a void space in the center, although a porous material would be suitable. A fully dense material is not a requirement of a solid sphere. It should be understood that a hollow sphere, as used herein, has at least one void space inside with a defined size and shape.
  • the template sphere can have a void volume % of at least 30%.
  • the template sphere can be formed from a glass or substantially glassy material.
  • the cenosphere can be a commercially produced ceramic or glass hollow sphere that is made as a side product in various industrial processes.
  • the term "sphere” is used, it is to be understood that the "sphere” can have irregular shapes (e.g., non- spheroidal) and, therefore, can be a consistently round spherical object or it can be less than perfect with respect to sphericity and/or roundness or can have other shapes.
  • the template sphere can have a Krumbein sphericity of at least about 0.3, such as at least 0.4, at least 0.5, at least 0.6, at least 0.7, such as from 0.3 to 0.9 or higher.
  • the template sphere alternatively, or in addition, can have a roundness of at least about 0.1, such as at least about 0.3, at least 0.4, at least 0.5, at least 0.7, such as from 0.1 to 0.9 or higher.
  • the overall proppant which can be the template sphere, alone or with one or more layers on the template, can have the same Krumbein sphericity and/or roundness values mentioned for the template.
  • the proppant can have a Krumbein sphericity of at least about 0.5 (such as at least 0.6, at least 0.7, at least 0.8, at least 0.9, such as from 0.5 to 0.9 or higher) and/or the proppant can have a roundness of at least about 0.4 (such as at least 0.5, at least 0.7, at least 0.8, such as from 0.4 to 0.9 or higher).
  • the proppant can have one or more layers located on the template sphere. At least one of these layers can form a shell around the entire outer surface of the template sphere.
  • the shell can be a continuous shell or a non-continuous shell.
  • the shell can have a thickness of from about 5 micrometers to 150 micrometers or thicker.
  • the shell can be sintered.
  • the shell can include ceramic.
  • the shell can include glass-ceramic.
  • the glass- ceramic or glass-ceramics can be present in one or more components (or parts) of the proppant.
  • the glass-ceramic can be present on at least the outer surface of the template sphere.
  • the glass-ceramic can be present on the entire circumference of the outer surface of the template sphere or a portion thereof.
  • the outer surface can comprise the exposed, outer most surface.
  • the presence of the glass-ceramic can include portions beneath this exposed surface, such as 0.1% to 100% of the inner volume or area of the template sphere, e.g., from 1% to 90%, from 5% to 80%, 10% to 70%, 15% to 60%, 20% to 50%, and the like.
  • the glass-ceramic can be distributed uniformly or non-uniformly in the outer surface and/or inner volume of the template sphere.
  • the glass-ceramic of the template sphere can be in solid form.
  • the glass-ceramic of the template sphere can be in porous or hollow form.
  • the glass-ceramic can be present uniformly throughout the shell or distributed non- uniformly in one or more portions of the shell.
  • the glass-ceramic of the shell can be in solid form.
  • the glass-ceramic of the shell can be in porous or hollow form.
  • the glass-ceramic of the shell can be the same or different from the glass-ceramic of the template sphere.
  • the glass-ceramic of the shell can have the same or different degree of crystallinity as the glass-ceramic of the template sphere, and/or the same or different composition as the glass-ceramic of the template sphere.
  • the glass-ceramic can comprise from about 0.5% by weight to about 100% by weight of the overall proppant, based on the total weight percent of the proppant.
  • the glass-ceramic can be present in an amount from about 5 wt% to about 90 wt% or higher, from about 10 wt% to about 75 wt%, from about 15 wt% to about 50 wt%, from about 20 wt% to about 30 wt% or higher, all based on the total weight of the proppant.
  • Glass-ceramic refers to any glass-ceramic that is formed when glass or a substantially glassy material is annealed at elevated temperature to produce a substantially crystalline material with limited crystallinity or controlled crystallite size.
  • limited crystallinity should be understood as crystallinity of from about 5% to about 100%, by volume (e.g., 10% to 90%; 20% to 80%; 30% to 70%; 40% to 60% by volume).
  • the crystallite size can be from about 0.01 micrometers to 20 micrometers, such as 0.1 to 5 micrometers. Preferably the crystallite size is less than 1 micrometer.
  • the glass-ceramic can be composed of aluminum oxide, silicon oxide, boron oxide, potassium oxide, zirconium oxide, magnesium oxide, calcium oxide, lithium oxide, phosphorous oxide, and/or titanium oxide or any combination thereof.
  • the glass-ceramic can comprise from about 35% to about 55% by weight Si0 2 ; from about 18% to about 28% by weight A1 2 0 3 ; from about 1% to about 15% by weight (e.g., 1 to 5 wt%) CaO; from about 7% to about 14% by weight MgO; from about 0.5% to about 15% by weight Ti0 2 (e.g., 0.5 to 5 wt%); from about 0.4% to about 3% by weight B 2 0 3 , and/or greater than 0% by weight and up to about 1% by weight P 2 0 5 , all based on the total weight of the glass- ceramic.
  • the glass-ceramic can comprise from about 3% to about 5% by weight Li 2 0; from about 0% to about 15% by weight A1 2 0 3 ; from about 10% to about 45% by weight Si0 2 ; from about 20% to about 50% by weight MgO; from about 0.5% to about 5% by weight Ti0 2 ; from about 15% to about 30% by weight B 2 0 3 , and/or from about 6% to about 20% by weight ZnO, all based on the total weight of the glass-ceramic.
  • the template sphere can comprise a mixture of aluminum oxide, silicon oxide, titanium oxide, iron oxide, magnesium oxide, calcium oxide, potassium oxide and/or sodium oxide, and/or any combination thereof.
  • the glass-ceramic can be fully or nearly fully crystalline or can contain a glass component (e.g., phase(s)) and a crystalline component (e.g., phase(s)) comprising crystallites.
  • the glass-ceramic can have a degree of crystallinity of from about 5% to about 100%, or from about 15% to about 80%.
  • the glass-ceramic can have from about 50% to 80%) crystallinity, from about 60% to 78% crystallinity or from about 70% to 75%» crystallinity by volume.
  • the crystallites can have a random and/or directed orientation.
  • the crystal orientation of the crystals in the glass-ceramic can be primarily random or can be primarily directed in a particular orientation(s) (e.g., non-random).
  • the crystal orientation of the glass-ceramic can be primarily random such that at least 50% or higher of the orientations are random orientations based on the overall orientation of the crystals present.
  • the random orientation can be at least 60%, at least 70%, at least 80%, at least 90%, such as from about 51% to 99%, from 60% to 90%, from 70% to 95% or higher with respect to the percent of the crystals that are random based on the crystals measured.
  • X-ray diffraction can be used to determine the randomness of the crystallites.
  • the glass-ceramic can have both crystal and glass components, the glass-ceramic can have certain properties that are the same as glass and/or crystalline ceramics.
  • the glass-ceramic can provide an ideal gradient interface between the template sphere and the ceramic shell, if present.
  • the glass-ceramic can be impervious to thermal shock.
  • the proportion of the glass and crystalline component of the glass-ceramic can be adjusted to match (e.g., within 10%, within 5%, within 1%, within 0.5%, within 0.1%) the coefficient of thermal expansion (CTE) of the shell or other material to which it will be bonded or attached or otherwise in contact with, in order to prevent premature fracture(s) resulting from cyclic stresses due to temperature changes, or thermal fatigue.
  • CTE coefficient of thermal expansion
  • the glass-ceramic has from 70% to 78% crystallinity, the two coefficients balance such that the glass-ceramic as a whole has a thermal expansion coefficient mismatch that is very close to zero.
  • the present invention can provide a proppant with improved stiffness and/or lower density.
  • the proppant of the present invention can be either a monolithic structure or a composite having a gradient interface between composite components, or a gradient in composite properties.
  • the proppant of the present invention has little or none of the stress associated with proppants having a distinct linear interface between dissimilar materials.
  • the stress, or internal locked stress, of the proppant can be measured by any suitable technique known in the art.
  • the stress of the proppant can be determined by X-ray diffraction peak profile analysis, for example.
  • the proppant of the present invention is therefore, less prone to fracture than conventional proppants.
  • the proppant can be a multi-phase system or a single-phase system. In a multi-phase system, such as a two phase system, the proppant can comprise a template sphere or core and a second phase(s) that can be different or dissimilar from the template sphere or core.
  • the second phase of the two-phase system can coat or encapsulate or act as a shell to the supporting or template first phase, and/or infiltrate (e.g., partially to optional varying degrees or gradients or completely) the supporting or template first phase, and/or react with the supporting or template first phase.
  • the template sphere can include, at least partially, glass or a glass-containing ceramic material.
  • the second phase can be a ceramic or glass-ceramic shell. The present inventors have found that a sharp interface between the shell and the template sphere of the proppant should be avoided in order to achieve a proppant with improved properties.
  • a sharp interface between a glassy template sphere and a ceramic shell can be avoided by crystallizing at least the outer surface of the template sphere, to form glass-ceramic, by providing a glass-ceramic layer between this interface, and/or by providing a shell that is at least partially glass-ceramic.
  • the glass-ceramic can serve as a functionally gradient material.
  • the glass-ceramic can permit a gradual transition of ratios between glass content and ceramic content, and thereby, a gradient in composite properties.
  • glass-ceramics can have improved properties compared to glass.
  • the proppant can achieve increased stiffness, improved fracture toughness, low thermal expansion coefficient, high hardness, high Young's Modulus, thermal stability, and/or high strength.
  • Sizes e.g., particle diameters
  • the particle diameter can be in the range of from 50 micrometers to 2,000 micrometers or 100 micrometers to 2000 micrometers.
  • the sizes of the template spheres e.g., particle diameters
  • the template sphere can, for example, have a diameter that is from about 20 micrometers to about 1000 micrometers, such 100 micrometers to 1000 micrometers.
  • the glass-ceramic in the proppant can be a mechanically strong material and can sustain temperatures of up to about 800° C to 1500° C.
  • the glass-ceramic can withstand temperature changes of 100° C in a span of one minute or less (e.g., 60 seconds to 1 second, 10 seconds to 50 seconds).
  • the glass-ceramic can have a density of from about 1.0 to about 3.5 g/cm 3 , such as 1.5, 2.0, 2.52, or 2.5 g/cm 3 .
  • the glass-ceramic can have a Young's Modulus of from about 50 to about 80 GPa, such as 68, 66.9, or 70 GPa.
  • the glass-ceramic can have a shear modulus (at 25° C) of from about 20 to about 50 GPa, such as 25 GPa or 25.5 GPa.
  • the glass- ceramic can have a modulus of rupture (at 25° C) of from about 50 to about 150 MPa, such as 60 MPa, 70 MPa, 80 MPa, or 100 MPa.
  • the glass-ceramic can have a compressive strength of from about 300 MPa to about 500 MPa, such as 360 MPa.
  • the glass-ceramic can have a fracture toughness of from about 1 to about 10MPa.m 1 2 , such as 1.52, 1.53, or 1.54 MPa.m 1 2 .
  • the glass- ceramic can have a thermal conductivity of 1.45 to about 1.53 W/(m-K) or higher, such as 1.47 W/(m-K).
  • the proppant can have properties similar to those described for the glass-ceramic.
  • the proppant can have at least one of the following properties: a density of from about 1.5 to about 3.0 g/cm 3 ; a Young's Modulus of from about 50 to about 80 GPa; a MOR (at 25° C) of from about 50 to about 150 MPa, such as 90 to 110 MPa, or 93 to 97 MPa; a shear modulus (at 25° C) of from about 20 to about 50 GPa; a compressive strength of from about 300 MPa to about 500 MPa; and/or a fracture toughness of about 1 to about 10 MPa.m 1/2 , such as 1.54 to about 1.55 MPa.m 172 .
  • the proppant can have a specific gravity of from about 1.0 to about 4.0.
  • the proppant can have a specific gravity of about 3 or less (e.g., 0.5 to 3, 0.8 to 2.5, 0.9 to 2.3, 1 to 2, 1.1 to 1.8, 1.2 to 1.7, from 0.8 to 2, and the like).
  • the proppant can have a coefficient of thermal expansion (CTE at from 25° C to 300° C) of from 0.1 x 10 "6 /K to 13 10 '6 K (e.g., 0.1 x 10 "6 /K to 12 ⁇ 10 "6 /K, 0.3 ⁇ 10 "6 /K to 5 ⁇ 10 "6 /K, 0.5 ⁇ 10 "6 /K to 1.0 10 " 6 /K, 0.75 x 10 "6 /K to 1.5 x 10 "6 /K).
  • the proppant can have a thermal conductivity of from about 0.01 W/(m-K) to 3.0 W/(m-K) (e.g. 1.45 W/(m-K) to about 1.47 W/(m-K)).
  • the proppants of the present invention can have a crush strength of 1,000 psi to 20,000 psi or higher (e.g., from 1,500 psi to 10,000 psi, from 3,000 psi to 10,000 psi, from 5,000 psi to 10,000 psi, from 9,000 psi to 12,000 psi). Other crush strengths below or above these ranges are possible.
  • the template sphere can have a coefficient of thermal expansion (CTE at from 25° C to 300° C) of from about 0.1 ⁇ 10 '6 /K to about 13 ⁇ 10 _6 / ⁇ , such as from 0.1 ⁇ 10- 6 /K to 2 ⁇ 10 _ 6 /K or 1.2 x 10 "6 /K to 1.7 * 10 "6 /K .
  • the template sphere can have a specific gravity of from 0.01 to about 3.
  • the template sphere can have a MOR of from about 1 to about 100 MPa, such as 10 to 90 MPa.
  • the amount of glass-ceramic present in the template sphere can be about 0.1% to 100% by weight of the template sphere.
  • the amount of glass-ceramic present in the template sphere can be from about 1% to about 90%, from about 10% to 80%», from about 20% to 70%, from about 30% to 60%, from about 40% to 50%, from about 5% to 75%, from about 50% to 70%, from about 65% to 85%, from about 15% to 65%, or from about 90% to 99% by weight of the template sphere, wherein all percents are percent by weight based on the weight of the template sphere.
  • the remaining portion of the template sphere can be made from glass or a mixture of glass and crystalline ceramic materials, and/or other materials, e.g., metal, metal oxides, and the like.
  • the template sphere may also include crystal initiators.
  • Crystal initiators can include, but are not limited to, alkali metals (or oxides thereof), such as, lithium, sodium, potassium, rubidium, cesium, and francium, as well as transition metals or oxides of transition metals, such as, scandium titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, yttrium, zirconium, niobium, molybdenum, technetium, ruthenium, rhodium, palladium, silver, cadmium, hafnium, tantalum, tungsten, rhenium, osmium, iridium, platinum, gold, mercury, rutherfordium, dubnium, seaborgium, bohrium, hassium, meitnerium, ununnilium, unununium, ununbium, or any combinations thereof.
  • the amount of crystal initiators present in the template sphere can be from about 0.1%-25% by weight, such as 0.1%-
  • Glass can be any inorganic, non-metallic solid non-crystalline material, such as prepared by the action of heat and subsequent cooling.
  • the glass can be any conventional glass such as, for example, soda-lime glass, lead glass, or borosilicate glass.
  • Crystalline ceramic materials, as used herein, can be any inorganic, non-metallic solid crystalline material prepared by the action of heat and subsequent cooling.
  • the crystalline ceramic materials can include, but are not limited to, alumina, zirconia, stabilized zirconia, mullite, zirconia toughened alumina, spinel, aluminosilicates (e.g., mullite, cordierite), perovskite, perchlorate, silicon carbide, silicon nitride, titanium carbide, titanium nitride, aluminum oxide, silicon oxide, zirconium oxide, stabilized zirconium oxide, aluminum carbide, aluminum nitride, zirconium carbide, zirconium nitride, iron carbide, aluminum oxynitride, silicon aluminum oxynitride, aluminum titanate, tungsten carbide, tungsten nitride, steatite, and the like, or any combination thereof.
  • the template sphere can have at least an outer surface that is glass-ceramic. For example, at least 1% to 100% (e.g., 10% to 90%, 20% to 70%, 0.5% to 5%, 1% to 5%, 2% to 10%, 1% to 20%, 5% to 30%, 5% to 40%, 10% to 50%) of the radius starting from the outer surface of the template sphere going to the center of the sphere, can be glass-ceramic.
  • the template sphere can include aluminum oxide, silicon oxide, iron oxide, magnesium oxide, calcium oxide, potassium oxide, etc., or mixtures thereof.
  • the glass-ceramic of the template sphere can have a thickness of any amount, such as from 1 micron to about 150 micrometers or from about 5 micrometers to about 120 micrometers.
  • the glass-ceramic can be formed to have a substantially uniform thickness around the template sphere.
  • the thickness of the glass-ceramic can be substantially uniform in thickness by not varying in thickness by more than 20% or more preferably by not varying more than 10% in overall thickness.
  • the glass-ceramic can be non-continuous or continuous. Continuous, for purposes of the present invention means that the entire outer surface of the template sphere is glass-ceramic. Preferably, at least the entire outer surface of the template sphere is glass-ceramic.
  • the outer surface can have a thickness of from about 0.1 to about 1000 ⁇ .
  • the degree of crystallinity in the glass-ceramic can vary from one portion of the template sphere to another portion of the template sphere.
  • the glass-ceramic forming the outer surface of the template sphere, or the portion of the template sphere nearest to the shell can have a greater crystallinity than glass-ceramic which is formed deeper (depth in the sphere) within the template sphere and further from the shell.
  • the crystallinity of the glass-ceramic beginning at the outer surface of the template sphere can be from about 10% to 100%, for example, and then progressively decrease as the glass-ceramic approaches the non-crystalline glass portion of the template sphere, ending at a crystallinity of from about 1% to 100%.
  • the template sphere can be entirely glass-ceramic.
  • the template sphere can be a cenosphere formed from both glass and ceramic, and have an outer surface that is glass ceramic.
  • the second phase as a layer or layers can coat the supporting or template first phase, and/or infiltrates the supporting or template first phase, and/or reacts with the supporting or template first phase.
  • the second phase or shell can be partially ceramic, partially glass-ceramic, entirely ceramic, or entirely glass-ceramic.
  • the shell can be crystalline or amorphous.
  • the shell can include an oxide, such as aluminum oxide called alumina.
  • the shell can include a silicon oxide, sodium oxide, potassium oxide, calcium oxide, zirconium oxide, aluminum oxide, lithium oxide, iron oxide, magnesium oxide, calcium oxide, cerium oxide, yttrium oxide, scandium oxide, titanium dioxide, cordierite, spinel, spodumene, steatite, a silicate, a substituted aluminosilicate clay or any combination thereof.
  • the shell can include a metal oxide, a metal carbide, a metal nitride, a metal boride, a metal silicide or any combination thereof, derived from any metal sources and any combination thereof.
  • the shell can include a mixed metal oxide of aluminum called an aluminate, a silicate, or an aluminosilicate, such as mullite or cordierite.
  • the shell can include an amorphous silica.
  • the aluminate or ceramic may contain magnesium, calcium, yttrium, titanium, lanthanum, barium, and/or silicon.
  • the ceramic may be formed from a nanoparticle precursor such as an alumoxane.
  • Alumoxanes can be chemically functionalized aluminum oxide nanoparticles with surface groups including those derived from carboxylic acids such as acetate, methoxyacetate, methoxyethoxyacetate, methoxyethoxyethoxyacetate, lysine, and stearate, and the like.
  • the shell may further include crystal initiators, such as Ti0 2 or Li 2 0.
  • the amount of crystal initiators present in the shell can be from about 0.1% to 25%, such as 1% to 15%, 3% to 13 wt%, 0.1% to 7%, 0.1% to 5%, or 0.1% to 3% by weight, based on the weight of the shell.
  • the shell can comprise one or more layers (e.g., two, three, four, five, or more layers). Each of the shell layers can vary in composition from an adjacent shell layer. For example, the amount of one or more components in each shell layer (if one or more are the same) can gradually increase or decrease from layer to layer. Additionally or alternatively, one or more components of one shell layer can be different from another shell layer.
  • the shell can have a coefficient of thermal expansion (CTE at from 25° C to 300° C) of from 0.1 ⁇ 10 "6 /K to 13 ⁇ 10 "6 /K, such as from 0.1 10 "6 /K to 12x 10 "6 /K or 1.2 ⁇ 10 "6 /K to 5 x 10 "6 /K.
  • CTE coefficient of thermal expansion
  • the proppants of the present invention can comprise a single particle or multiple particles and can be a solid, partially hollow, partially hollow and randomly distributed or completely ho,llow in the interior of the particle.
  • the particle can be spherical, nearly spherical, polygonal, oblong in shape (or any combination thereof) or have other shapes suitable for purposes of being a proppant.
  • the proppant can also be in the shape of, for example, rods, pillars, spikes, gears, donuts, cylinders, or peanuts.
  • the desired proppant shape can be achieved in any suitable manner.
  • the desired proppant shape can be achieved using, for example, extrusion, granulation, fluid bed coating, a fluid bed granulator, a fluid spray dryer, or a pelletizer, such as an Eirich mixer.
  • the particles can have any aspect ratio (L/D), such as from 2: 1 to 1 :2 (e.g., 1.2: 1 to 1 : 1.12, such as 1 : 1 or about 1 : 1).
  • L/D aspect ratio
  • the overall proppant can have any particle size.
  • the proppant can have a particle diameter size of from about 90 micron to about 2 mm, or a diameter of from about 90 micrometers to about 20,000 micrometers, or a diameter of from about 100 micrometers to about 2,000 micrometers, or a diameter of from about 200 micrometers to about 1000 micrometers.
  • Other particle sizes can be used.
  • the particle sizes as measured by their diameter can be above the numerical ranges provided herein or below the numerical ranges provided herein.
  • the proppant in a single-phase system, can comprise a sphere, but does not include a second phase as a shell that is different or dissimilar from the template sphere or core.
  • the sphere in the single-phase system can have the same composition and dimensions, as the template sphere of the multi-phase system, described above.
  • the sphere of the single-phase system can have at least an outer surface that is glass-ceramic.
  • the sphere of the single-phase system can be entirely glass-ceramic.
  • the sphere of the single-phase system can, for example, have a composition of from about 44% to 48% Si0 2 , 14% to 18% A1 2 0 3 , 5% to 10% B 2 0 3 , 8% to 12% K 2 0, and 13% to 18% MgO, all weight percents that are based on the total weight of the sphere.
  • the sphere of the single-phase system can have 46 wt% Si0 2 , 16 wt% A1 2 0 3 , 7 wt% B 2 0 3 , 10 wt% K 2 0, and 17 wt% MgO, based on the weight of the sphere.
  • the proppants of the present invention can be used to prop open subterranean formation fractions.
  • the proppant can be suspended in a liquid phase or other medium to facilitate transporting the proppant down the well to a subterranean formation and placed such as to allow the flow of hydrocarbons out of the formation.
  • the medium chosen for pumping the proppant can be any desired medium capable of transporting the proppant to its desired location including, but not limited to, a gas and/or liquid, energized fluid, foam, like aqueous solutions, such as water, brine solutions, and/or synthetic solutions.
  • Any of the proppants of the present invention can have a crush strength sufficient for serving as a proppant to prop open subterranean formation fractures.
  • the crush strength can be 1,000 psi or greater, 3,000 psi or greater, greater than 4,000 psi, greater than 9,000 psi, or greater than 12,000 psi.
  • Suitable crush strength ranges can be from about 3,000 psi to about 20,000 psi, or from about 5,000 psi to about 20,000 psi, and the like.
  • a crush strength below 3,000 psi can be useful, such as 500 psi to 3,000 psi, or 1,500 psi to 2,000 psi.
  • the proppant can be suspended in a suitable gas, foam, energized fluid, or liquid phase.
  • the carrier material, such as a liquid phase is generally one that permits transport to a location for use, such as a well site or subterranean formation.
  • the subterranean formation can be one where proppants are used to improve or contribute to the flow of hydrocarbons, natural gas, or other raw materials out of the subterranean formation.
  • the present invention also relates to a well site or subterranean formation containing one or more proppants of the present invention.
  • the preparation of the glass-ceramic can involve heat treating a glass article at a temperature where crystal nuclei are allowed to form in the glass and treating the glass article at a temperature where the crystallites of the desired phases are allowed to grow to a desired extent.
  • the crystalline grains of the glass-ceramic can be annealed from a glass or substantially glass sphere or template sphere. Annealing induces nucleation of one or more crystalline phases. Nucleation may be accelerated by seeding the glass with crystal initiators, such as titanium dioxide and/or lithium oxide.
  • Annealing is completed when the intended level of crystallinity is reached, typically from 1% to 100%, from 15% to 80%, from 50% to 80%, from 60% to 78% and from 70% to 75%, in weight percents by weight of the article (e.g., template sphere or layer).
  • the template sphere can be formed from a glass or substantially glassy material.
  • the template sphere can be a glass or glass-like hollow sphere.
  • the glass sphere can be either partially or entirely converted to glass-ceramic upon heating of the glass sphere or upon sintering of the shell.
  • Temperature can be regulated by introducing a temperature gradient and degree of cooling or first heating, then cooling and followed by a heating to promote glass-ceramic formation or conversion. It is also possible to achieve an oriented crystal alignment, however, which may further enhance stiffness.
  • crystalline grains nucleate, begin to grow, and ultimately comprise a majority of the material.
  • High melting point compounds or crystal initiators can facilitate nucleation and/or act as a catalyst.
  • the nucleation temperature is a temperature at which crystals begin to form and grow within the glass.
  • the selected nucleation temperature should be below a temperature at which the glass would thermally deform. Below its melting temperature, a crystal typically has significantly lower thermal deformation than a corresponding glass.
  • the crystal initiators can be in the form of a solid powder.
  • the particle size of the powder can be modified by milling.
  • the crystal initiators can, alternatively, be in liquid form.
  • the crystal initiators can be derived from precursors that convert to oxide from either liquid, solid or gaseous forms.
  • the precursors can include, TiCl 4 , LiCl, Ti(OC 2 H 5 ) 4 , or Li(OH).
  • the oxides convert partially or entirely, to glass-ceramic.
  • the shell can be formed from a silica, an alumina, and/or other ceramics, such as cordierite and mullite.
  • the silica can be, for example, an amorphous silica. Crystal initiators may be used to facilitate converting the amorphous silica or alumina to oxides.
  • the shell can be applied to the template sphere before or after the template sphere has achieved the desired crystallinity.
  • the shell can be formed on the template sphere once the template sphere is comprised at least partially of glass-ceramic.
  • the shell coating can be applied to the surface of a glass template sphere prior to crystallization of the template sphere.
  • the template sphere can be coated with the shell coating and sintered. Upon heat treatment of the composite shell and template sphere, any glass material in the shell as well as glass in the template sphere can be partially, or entirely converted to a glass-ceramic.
  • the shell can be formed from ceramics, such as cordierite and/or mullite, and/or with crystal initiators, such as Ti0 2 or Li 2 0.
  • the crystal initiators can be added to a coating slurry as a solid powder, or as liquid, solid, or gaseous precursors which convert to oxides. If a solid powder is used, the size of the powder particles can be controlled by milling.
  • the precursors can be, for example, TiCl 4 , LiCl 2 , Ti (OC 2 H 5 ) 4 , and/or Li(OH).
  • the template sphere can be coated with the ceramic shell coating and sintered.
  • the sintered ceramic grain size can be less than 1 micron, such as 0.1 to 0.8 micrometers, or 0.2 to 0.5 micrometers.
  • the shell can be formed from amorphous silica and/or alumina.
  • the amorphous silica and/or alumina are glass-ceramic precursors which, with the addition of crystal initiators, can be converted to oxides.
  • the oxides, once obtained, can convert, entirely, or at least partially to glass-ceramic.
  • the shell can be formed from glass-ceramic precursors and other ceramics, such as cordierite or mullite.
  • the composite of the glass-ceramic precursors and ceramic materials in the shell can be heat treated with the template sphere. Upon heating, the glass materials in the template sphere and shell can be converted entirely, or at least partially to glass-ceramic.
  • the shell can be prepared from one or more different coating slurries to form one or more shell layers on the template sphere.
  • At least one coating slurry can include ceramic materials, such as cordierite or mullite. Crystal initiators can be added into the coating slurry.
  • a spray coater may be programmed to alternately spray from at least two different coating slurries onto the template. After coating the template sphere with at least two different coating slurries, the proppant can be heated to achieve a layered shell structure. During heating, the top shell layer is exposed to more heat than the underlying shell layers and the template sphere. As such, small-glass ceramic particles which can form in the top shell layer can fuse together and result in a dense top layer.
  • the substrate or template preferably prior to the optional second phase or optional coating or optional shell being present, can be treated in one or more ways to remove or diminish flaws on the surface of the substrate or template.
  • These flaws may be convex or concave in nature or both. This can be especially beneficial when the template or substrate is an inorganic material.
  • the removal or diminishing of these flaws, especially strength-limiting flaws, can permit the second phase or coating or shell to provide more enhanced strengthening of the substrate or template and the overall proppant.
  • the flaws can include, but are not limited to, peaks, protuberances, ridges, craters, and other flaws which can include surface undulations, which are significantly different from the overall surface texture or surface smoothness of the substrate or template.
  • a flaw in a material system can be considered as anything which negatively impacts the apparent strength of a material system.
  • Flaws can be physical and/or chemical in nature. Physical flaws may include such things as protuberances, bumps, scratches, grooves, pores, pits, dislocations, and/or defects in the crystal structure of the material. Chemical flaws may include phases that prevent solid state bonding, e.g. grain boundary phases, modification of the crystal structure through atomic substitution, and the like.
  • the sharp protuberances or peaks or ridges can be removed or diminished, and a surface can be created that is "smoother and more spherical" which can permit the second phase or coating or shell to be more effective in providing strength to the overall proppant.
  • a surface can be created that is "smoother and more spherical" which can permit the second phase or coating or shell to be more effective in providing strength to the overall proppant.
  • an aspect ratio (AR) test can be used and/or the radius of curvature (RC) can be compared.
  • the AR can be 5 or less, such as from 0.1 to 5, or from 0.2 to 5, or from 0.5 to 5, or from 0.1 to 4, or from 0.1 to 3, or from 0.1 to 2, or from 0.8 to 1, or from 0.1 to 1.8, or from 0.1 to 1.5, or from 0.5 to 1.3, or from 0.7 to 1.2 and other ranges.
  • the AR is about 1.
  • the RC can typically range from 0.5 ⁇ to 100 ⁇ , with the upper limit of the radius of curvature being the radius of the template.
  • various devices and methods can be used which provide sufficient temperature to allow crystallization to occur.
  • These devices and/or methods include, but are not limited to, static bed furnaces, dynamic bed furnaces (e.g., rotating tube furnaces), fluidized bed furnaces, direct injection into high temperature flames (for instance, oxidizing flames), use of a gas flame contained within a combustion tube mounted vertically and/or injection into a high temperature plasma flame.
  • the template sphere can be heated to any temperature sufficient to crystallize all or a portion of the template sphere, for instance, to temperatures of from about 300° C to 1,300° C or 500° C to 1,500° C.
  • the heat treatment can occur for any time sufficient to crystallize all or a portion of the template sphere.
  • the heat treatment can occur for a period of, for example, 10 minutes to 50 hours or more, such as 2 hours to 10 hours.
  • pressures can be used to control the template structure or the physical properties of the template. For instance, pressures may be used from less than 0.1 atm to 10 atm or greater, such as from 1 atm to 5 atm.
  • the localized pressure is reduced to values below that of ambient pressure, this can lead to the expansion of the template and consequently a reduction in the density of the template.
  • the localized pressure is increased above ambient pressure, this can result in the contraction of the template to smaller overall diameters and hence an increase in the density of the template.
  • this technique provides the ability to "dial in” or control certain densities of the proppant material.
  • the reduction or increase in pressure can improve the morphology of the template, especially when the template is held or is very near the glass transition temperature of the template material.
  • the change in localized pressure can be achieved through the use of various pressure control devices and techniques, such as a sealed ceramic tube surrounded by heating elements and containing the template material, wherein the ceramic tube is connected to either a pressure source or sink.
  • Pressurizing fluid can be used to achieve the desired localized pressure, such as air, nitrogen, inert gases, such as argon, or any gas.
  • crystal initiators Prior to heat treatment, it is an option to include crystal initiators, as described elsewhere herein, in order to facilitate crystallization of the glass.
  • Heat treatment may also be carried out in alternate atmospheres, other than that of air to induce the formation of new phases, for example thermal treatment in a nitriding atmosphere to form the nitrides, or thermal treatment in a carburizing atmosphere to form the carbides.
  • atmospheres include inert gases, carbon monoxide, nitrogen, nitrogen oxide, nitrogen dioxide, dinitrogen pentoxide, anhydrous ammonia, and the like.
  • the properties of the template or substrate may be modified by way of pressure and/or temperature effects.
  • a variation in pressure with the application of thermal energy may be used to alter the specific gravity of the template material.
  • the template and/or the shell can be surface modified, such as with the addition of silicon oxide, sodium oxide, potassium oxide, calcium oxide, zirconium oxide, aluminum oxide, lithium oxide, iron oxide, cordierite, spinel, spodumene, steatite, a silicate, an alumino silicate material, an aluminum containing material, a silicon containing material, an aluminum-silicon containing material, a substituted alumino silicate clay or any combination thereof.
  • the shell can be surface modified, for instance, by the addition of one or more inorganic materials or phases, or the attachment (e.g., chemical attachment or bonding) of one or more chemical groups, such as hydrophilic groups or hydrophobic groups.
  • the chemical groups can be surfactants, polymers, ionic groups, ionizable groups, acid groups, salts, surface active agents, and the like.
  • the surface modification can improve the surface morphology of the proppant, especially after the proppant is a sintered proppant.
  • the inorganic material or phases used for surface modification can include glassy materials, such as silicon oxide, alone or with the addition of oxides of sodium, potassium, calcium, zirconium, aluminum, lithium, iron, or any combination thereof.
  • the amount of the silicon oxide can be from about 70 wt% to about 99 wt%, such as from about 85 wt% to about 95 wt%, and the addition of the one or more other oxides, such as sodium oxide and the like, can be from about 1 wt% to about 15 wt%, such as from about 2 wt% to about 10 wt%.
  • the surface modification of the shell can include the application of one or more organic materials (e.g., aliphatic compounds, ionic compounds, surfactants, aromatic compounds, polymeric compounds) or the application of an organic phase(s).
  • the organic material or chemical groups can be bonded to the shell surface or adsorbed, or absorbed or otherwise attached.
  • the organic material or organic phase can modify the proppant's propensity to interact with aqueous solutions, thus making the proppant either hydrophobic, hydrophilic, or hydro-neutral.
  • the surface modification of the shell can include the use of substances that are effectively activated by temperature elevation of the proppant to yield a modification of the proppant transport fluid (e.g., breaking the gel used to transport the proppant through the subterranean regions).
  • the surface treating which can occur after sintering of the proppant, can have the ability to improve one or more chemical and/or mechanical properties, such as enhanced transportability.
  • the template or substrate and/or shell can be modified, such as surface modified, through a variety of techniques.
  • the surface of the template or substrate can be modified through one or more heat treatments prior to the formation of the shell on the template.
  • Another form of surface treatment can be to modify chemically the surface of the template, such as by glazing, application of a bond coat, or chemical etching.
  • the chemical modification can improve the performance and/or stabilize the template surface. Removal of residual impurities, cleaning of the surface, reduction of residual stain distributions prior to coating, increasing the microscopic roughness of the surface to improve coating bond strength or removing and/or improving the morphology of protuberances.
  • the modification can be achieved by the preferential removal of one or more constituent phases on the template. For example, a wash with caustic soda may dissolve silica from the template.
  • the present invention includes the following aspects/embodiments/features in any order and/or in any combination:
  • a proppant comprising a template sphere, said template sphere having a Krumbein sphericity of at least about 0.3 and a roundness of at least about 0.1, said proppant having a Krumbein sphericity of at least about 0.5 and a roundness of at least about 0.4, and a continuous sintered shell around the entire outer surface of said template sphere, wherein at least the outer surface of said template sphere comprises a glass-ceramic or a glass-ceramic containing layer in contact with said outer surface of said template sphere.
  • glass-ceramic comprises crystallites having an orientation that is random.
  • glass-ceramic comprises crystallites having an orientation that is non-random.
  • said template sphere has a coefficient of thermal expansion (CTE at from 25° C to 300° C) of from 0.1 x 10 "6 /K to 13 ⁇ 10 "6 /K ; and/or
  • said shell has a coefficient of thermal expansion (CTE at from 25° C to 300° C) of from 0.1 ⁇ 10 "6 /K to 13 ⁇ 10 "6 /K .
  • CTE coefficient of thermal expansion
  • said proppant has a specific gravity of about 3 or less; and/or a coefficient of thermal expansion (CTE at from 25° C to 300° C) of from about 0.1 ⁇ 10 "6 /K to about 13 ⁇ 10 "6 /K ; and/or a thermal conductivity of from about 0.01 W/m-K to about 3.0 W/m-K.
  • the glass-ceramic has at least one of the following properties: a density of from about 1.5 to about 3.5 g/cm 3 ; a Young's Modulus of from about 50 to about 80 GPa; and/or a MOR of from about 50 to about 150 MPa.
  • template sphere has a MOR of from about 1 to about 100 MPa.
  • a fracture toughness of from about 1 to about 10 MPa.m 1/2 ; or e) a thermal conductivity of from about 0.01 to about 3 W7(m-K).
  • template sphere comprises a mixture of aluminum oxide, silicon oxide, titanium oxide, iron oxide, magnesium oxide, calcium oxide, potassium oxide and sodium oxide.
  • glass-ceramic of said template sphere comprises aluminum oxide, silicon oxide, boron oxide, potassium oxide, zirconium oxide, magnesium oxide, calcium oxide, titanium oxide or any combination thereof.
  • glass-ceramic of said template sphere comprises from about 10% to about 55% by weight Si0 2 ; from about 0% to about 28% by weight A1 2 0 3 ; from about 1% to about 5% by weight CaO; from about 7% to about 50% by weight MgO; from about 0.5% to about 25% by weight Ti0 2 ; from about 0.4% to about 30% by weight B 2 0 3 , and greater than 0% and up to about 5% by weight P 2 0 5 , based on the weight of the glass-ceramic.
  • glass-ceramic of said template sphere comprises from about 3% to about 10% by weight Li 2 0; from about 0% to about 28% by weight A1 2 0 3 ; from about 10% to about 55% by weight Si0 2 ; from about 7% to about 50% by weight MgO; from about 0.5% to about 25% by weight Ti0 2 ; from about 0.4% to about 30% by weight B 2 0 3 , and from about 6% to about 20% by weight ZnO, based on the weight of the glass-ceramic.
  • proppant of any preceding or following embodiment/feature/aspect wherein the proppant is rod-, pillar-, spike-, gear-, donut-, cylinder-, polygon- or peanut-shaped.
  • a proppant comprising a sphere, said sphere having a Krumbein sphericity of at least about 0.3 and a roundness of at least about 0.1, said proppant having a Krumbein sphericity of at least about 0.5 and a roundness of at least about 0.4, wherein at least the outer surface of said sphere comprises a glass-ceramic or a glass-ceramic containing layer in contact with said outer surface of said sphere.
  • glass-ceramic comprises crystallites having an orientation that is non-random.
  • said template sphere has a coefficient of thermal expansion (CTE at from 25° C to 300° C) of from about 0.1 ⁇ 10 "6 /K to about 13 x 10 " 6 /K .
  • proppant of any preceding or following embodiment/feature/aspect wherein the proppant has at least one of the following properties: a density of from about 1.5 to about 3.0 g/cm 3 ; and/or a Young's Modulus of from about 50 to about 80 GPa; and/or a MOR of from about 50 to about 150 MPa
  • proppant of any preceding or following embodiment/feature/aspect wherein said proppant has at least one of the following properties; shear modulus (at 25° C) of from about 20 to about 50 GPa; a modulus of rupture (at 25° C) of from about 50 to about 150 MPa; a compressive strength of from about 300 MPa to about 500 MPa; a fracture toughness of from about 1 to about 10 MPa. m 1/2 ; a thermal conductivity of from about 0.01 to about 3 W/(m-K).
  • proppant of any preceding or following embodiment/feature/aspect wherein said proppant comprises from about 10% to about 55% by weight Si0 2 ; from about 0% to about 28% by weight A1 2 0 3 ; from about 1% to about 5% by weight CaO; from about 7% to about 50% by weight MgO; from about 0.5% to about 25% by weight Ti0 2 ; from about 0.4% to about 30% by weight B 2 0 3 , and greater than 0% and up to about 5% by weight P 2 0 5 , based on the weight of the glass-ceramic.
  • a method of forming the proppant comprising providing a template sphere comprising glass; optionally hardening the template sphere; crystallizing at least an outer surface of said template sphere by heat treatment to form an outer surface comprising glass-ceramic; and, optionally, providing a shell around the entire outer surface of said template sphere; and sintering said shell to form a continuous sintered shell.
  • a proppant comprising a template sphere, said template sphere having a Krumbein sphericity of at least about 0.3 and a roundness of at least about 0.1, said proppant having a Krumbein sphericity of at least about 0.5 and a roundness of at least about 0.4, and a continuous sintered shell around the entire outer surface of said template sphere, wherein at least the continuous sintered shell comprises a glass-ceramic.
  • the present invention can include any combination of these various features or embodiments above and/or below as set forth in sentences and/or paragraphs. Any combination of disclosed features herein is considered part of the present invention and no limitation is intended with respect to combinable features.
  • a proppant according to the present invention can be prepared by coating conventional glass cenospheres with alkali metals.
  • the alkali metals can be dip-coated, spin coated, and spray-coated onto the glass cenospheres.
  • the cenospheres can be doped with transitional metal oxides. Once the cenospheres are coated or doped, as described, they are subjected to heat treatment for crystallization.
  • the cenospheres are heated to temperatures of 500° C to 1,000° C for a period of time sufficient to crystallize at least an outer surface of the cenospheres.
  • the amount of time in which the cenospheres are heated can vary depending on the degree of crystallization desired.
  • the cenospheres can be heated, for example, for a period of about 30 minutes to 12 hours, or from 2 hours to 10 hours. If full crystallization of the cenospheres is desired, the cenospheres should be heated for a fraction of an hour to several hours, for example, 0.1 to 10 hours or more.
  • the cenospheres can be coated with a ceramic shell, such as cordierite.
  • the cordierite can be granulated or pelletized through a granulator to achieve particles of about 200 micrometers in diameter or larger.
  • the formed cordierite particles are then dried and used to coat the cenospheres which have at least a glass- ceramic outer layer.
  • the cenospheres are then sintered.
  • the sintering can be conducted in a conventional manner, known in the art.
  • the coated cenospheres can be fired at temperatures of about 1,200° C to about 1,450° C, preferably 1,250° C to 1,420° C to form a sintered cordierite proppant.
  • additional proppants were prepared using the first cenosphere powder in Table 1 with cordierite.
  • the mixture (before taking into account the amount of the Ti0 2 present) was composed of 25 wt% cenosphere powder and 75 wt% cordierite and this mixture was formed into spheres, with the indicated additions of Ti0 2 , and sintered at 1260°C for 6 h.
  • the density and strength data of the samples are set forth in Table 3.
  • the splitting strength of the composite increased gradually with the content of the Ti0 2 and reached the maximum at 7 wt% Ti0 2 .
  • the amount of Ti0 2 is based on the total weight of the pellet or sphere.
  • the strength at this Ti0 2 level was more than doubled (108% net strength increase over the control) higher than the sample without any Ti0 2 .
  • the strength increase is mainly attributed to the glass-ceramic formation in the cenosphere powder.
  • the strength of these 1260°C sintered composite samples increased and then reached a maximum point and then dropped down, although the density kept increasing. This is so because when the Ti0 2 reached a certain level, further increasing of Ti0 2 would simply decrease the relative content of cenosphere powder. Again, this indicates the contribution of glass-ceramics from the cenosphere in the composite.
  • the microstructures of the composites of 25%:75% cenosphere- cordierite matrix without and with 7 wt% Ti0 2 are shown in Figure 4. It is seen that the sample with 7 wt% Ti0 2 is denser than without Ti0 2.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Ceramic Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Structural Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Geology (AREA)
  • Mining & Mineral Resources (AREA)
  • Physics & Mathematics (AREA)
  • Environmental & Geological Engineering (AREA)
  • Fluid Mechanics (AREA)
  • Glass Compositions (AREA)
  • Surface Treatment Of Glass (AREA)
PCT/US2010/060029 2009-12-22 2010-12-13 A proppant having a glass-ceramic material WO2011078985A1 (en)

Priority Applications (8)

Application Number Priority Date Filing Date Title
EP10839988.2A EP2516152A4 (en) 2009-12-22 2010-12-13 RETAINING AGENT COMPRISING A VITRO CERAMIC MATERIAL
CN201080064478.0A CN102781663B (zh) 2009-12-22 2010-12-13 具有玻璃-陶瓷材料的支撑剂
IN5062DEN2012 IN2012DN05062A (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html) 2009-12-22 2010-12-13
CA2785366A CA2785366C (en) 2009-12-22 2010-12-13 A proppant having a glass-ceramic material
MX2012007248A MX2012007248A (es) 2009-12-22 2010-12-13 Un consolidante que tiene un material de vidrio-ceramica.
AU2010333894A AU2010333894B2 (en) 2009-12-22 2010-12-13 A proppant having a glass-ceramic material
BR112012015322A BR112012015322A2 (pt) 2009-12-22 2010-12-13 propante e método para formar o propante
EA201290543A EA201290543A1 (ru) 2009-12-22 2010-12-13 Расклинивающий агент, содержащий стеклокерамический материал

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US28901409P 2009-12-22 2009-12-22
US61/289,014 2009-12-22

Publications (1)

Publication Number Publication Date
WO2011078985A1 true WO2011078985A1 (en) 2011-06-30

Family

ID=44149464

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2010/060029 WO2011078985A1 (en) 2009-12-22 2010-12-13 A proppant having a glass-ceramic material

Country Status (13)

Country Link
US (1) US8178476B2 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
EP (1) EP2516152A4 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
KR (1) KR20120105536A (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
CN (1) CN102781663B (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
AR (1) AR081515A1 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
AU (1) AU2010333894B2 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
BR (1) BR112012015322A2 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
CA (1) CA2785366C (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
EA (1) EA201290543A1 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
IN (1) IN2012DN05062A (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
MX (1) MX2012007248A (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
MY (1) MY162476A (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
WO (1) WO2011078985A1 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105452193A (zh) * 2013-08-07 2016-03-30 哈利伯顿能源服务公司 支撑剂及其制备方法

Families Citing this family (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2627727A4 (en) 2010-10-13 2015-10-28 Oxane Materials Inc IMPROVED RESISTANCE LIGHTWEIGHT SUPPORT AGENT AND METHODS OF MAKING THE SAME
US9227874B2 (en) * 2011-01-25 2016-01-05 Halliburton Energy Services, Inc. Extrusion process for proppant production
AU2012236861A1 (en) * 2011-03-29 2013-10-31 Saint-Gobain Ceramics & Plastics, Inc. Ceramic particle and process for making the same
BR112014000763A2 (pt) * 2011-07-13 2017-02-14 Oxane Mat Inc propantes de baixo atrito superficial
CN102531403B (zh) * 2011-12-01 2014-04-23 杭州市城市建设科学研究院 一种在空心玻璃微珠表面包覆堇青石的制备方法
US9663708B2 (en) 2012-08-01 2017-05-30 Halliburton Energy Services, Inc. Synthetic proppants and monodispersed proppants and methods of making the same
US9938452B2 (en) * 2012-10-24 2018-04-10 Halliburton Energy Services, Inc. Immobile proppants
US9102560B2 (en) * 2013-01-17 2015-08-11 Sibelco Asia Pte. Ltd. Charging load for making TFT glass and method of making same
CN103193461B (zh) * 2013-03-29 2016-09-21 杨松 利用镁矿、硼矿和铁矿的尾矿制备的支撑剂及其制备方法
US9714929B2 (en) 2013-04-02 2017-07-25 Halliburton Energy Services, Inc. Method to classify and select proppants
CA2849415C (en) 2013-04-24 2017-02-28 Robert D. Skala Methods for fracturing subterranean formations
US9828844B2 (en) 2013-05-07 2017-11-28 BAKER HUGHTES, a GE company, LLC Hydraulic fracturing composition, method for making and use of same
US9809742B2 (en) 2013-05-07 2017-11-07 Baker Hughes, A Ge Company, Llc Hydraulic fracturing composition, method for making and use of same
US9796914B2 (en) 2013-05-07 2017-10-24 Baker Hughes Incorporated Hydraulic fracturing composition, method for making and use of same
CA2914332A1 (en) * 2013-06-03 2014-12-11 Imerys Oilfield Minerals, Inc. Proppants and anti-flowback additives including compositions comprising calcium, multi-foil cross-sections, and/or size ranges
WO2015023612A2 (en) 2013-08-15 2015-02-19 Oxane Materials, Inc. Additive fabrication of proppants
AU2014321293B2 (en) 2013-09-20 2017-10-19 Baker Hughes, A Ge Company, Llc Method of using surface modifying treatment agents to treat subterranean formations
US9701892B2 (en) 2014-04-17 2017-07-11 Baker Hughes Incorporated Method of pumping aqueous fluid containing surface modifying treatment agent into a well
CN105555908B (zh) 2013-09-20 2019-10-08 贝克休斯公司 使用表面改性金属处理剂处理地下地层的方法
EP3046987B8 (en) 2013-09-20 2019-06-26 Baker Hughes, a GE company, LLC Use of organophosphorus containing composites for use in well treatment operations
BR112016005841B1 (pt) 2013-09-20 2022-02-08 Baker Hughes Incorporated Compósitos e métodos para tratamento de um poço, e propante, ou particulado de controle de areia
WO2015042488A2 (en) 2013-09-20 2015-03-26 Baker Hughes Incorporated Method of inhibiting fouling on a metallic surface using a surface modifying treatment agent
US9745508B2 (en) 2014-02-28 2017-08-29 University of Pittsburgh—of the Commonwealth System of Higher Education Proppants for sequestering a target species and methods of sequestering a target species in a subterranean formation
US10180037B2 (en) 2014-08-13 2019-01-15 Geodynamics, Inc. Wellbore plug isolation system and method
US9752406B2 (en) 2014-08-13 2017-09-05 Geodynamics, Inc. Wellbore plug isolation system and method
US9062543B1 (en) 2014-08-13 2015-06-23 Geodyanmics, Inc. Wellbore plug isolation system and method
CN106795062A (zh) * 2014-10-24 2017-05-31 哈里伯顿能源服务公司 制造陶瓷支撑剂的方法
USD754911S1 (en) * 2015-03-05 2016-04-26 Bocci Design and Manufacturing Inc Glass pendant for decorative light fixtures
CN106883838A (zh) * 2017-04-07 2017-06-23 山东雅丽支撑新材料科技有限公司 一种超低密度高强度的玻化瓷球支撑剂及其制备方法
CN109400952A (zh) 2017-08-18 2019-03-01 臻鼎科技股份有限公司 无机壳体、树脂组合物及无机壳体的制备方法
TWI626265B (zh) * 2017-08-21 2018-06-11 臻鼎科技股份有限公司 無機殼體、樹脂組合物及無機殼體的製備方法
CN107759206A (zh) * 2017-11-16 2018-03-06 深圳市大擎科技有限公司 耐高压陶瓷球壳、制备方法及深海浮力装置
CN108275987B (zh) * 2018-02-27 2020-05-19 重庆长江造型材料(集团)股份有限公司 一种表面改性石英砂及其制备方法
CN110877974A (zh) * 2018-09-06 2020-03-13 西安交通大学 一种低密度、高强度陶瓷球及其制备方法
FR3087195B1 (fr) * 2018-10-11 2022-01-28 Safran Aircraft Engines Procede de fabrication d'un revetement abradable poreux en materiau ceramique
US11155751B2 (en) * 2019-01-22 2021-10-26 Baker Hughes Holdings Llc Method of treating subterranean formations with composites having enhanced strength
CN114659554B (zh) * 2022-03-01 2023-04-25 安徽农业大学 一种生物质颗粒机故障诊断方法
CN114524617B (zh) * 2022-03-31 2023-11-28 郑州圣莱特空心微珠新材料有限公司 一种碳化硅改性的高导热、低介电中空玻璃微珠及其制备方法

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4440866A (en) * 1980-07-07 1984-04-03 A/S Niro Atomizer Process for the production of sintered bauxite spheres
US4654266A (en) * 1985-12-24 1987-03-31 Kachnik Joseph L Durable, high-strength proppant and method for forming same
US20070166541A1 (en) * 2005-02-04 2007-07-19 Smith Russell J Composition and method for making a proppant

Family Cites Families (175)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3365315A (en) 1963-08-23 1968-01-23 Minnesota Mining & Mfg Glass bubbles prepared by reheating solid glass partiles
US3888957A (en) 1972-02-03 1975-06-10 Philadelphia Quartz Co Method of making hollow spheres by spray drying
US3796777A (en) 1972-02-03 1974-03-12 Philadelphia Quartz Co Method of making hollow spheres by spray drying
US3794503A (en) 1972-05-12 1974-02-26 Philadelphia Quartz Co Hollow spheres consisting of alkali metal silicate and a polysalt
US3960583A (en) 1974-05-02 1976-06-01 Philadelphia Quartz Company Method of preparing modified hollow, largely spherical particles by spray drying
US4111713A (en) 1975-01-29 1978-09-05 Minnesota Mining And Manufacturing Company Hollow spheres
US4349456A (en) 1976-04-22 1982-09-14 Minnesota Mining And Manufacturing Company Non-vitreous ceramic metal oxide microcapsules and process for making same
US4743545A (en) 1984-08-09 1988-05-10 Torobin Leonard B Hollow porous microspheres containing biocatalyst
US5212143A (en) 1978-08-28 1993-05-18 Torobin Leonard B Hollow porous microspheres made from dispersed particle compositions
US4303061A (en) 1978-08-28 1981-12-01 Torobin Leonard B Solar energy collector having hollow microspheres
US4637990A (en) 1978-08-28 1987-01-20 Torobin Leonard B Hollow porous microspheres as substrates and containers for catalysts and method of making same
US4303432A (en) 1978-08-28 1981-12-01 Torobin Leonard B Method for compressing gaseous materials in a contained volume
US4671909A (en) 1978-09-21 1987-06-09 Torobin Leonard B Method for making hollow porous microspheres
US4777154A (en) 1978-08-28 1988-10-11 Torobin Leonard B Hollow microspheres made from dispersed particle compositions and their production
US4303433A (en) 1978-08-28 1981-12-01 Torobin Leonard B Centrifuge apparatus and method for producing hollow microspheres
US4793980A (en) 1978-09-21 1988-12-27 Torobin Leonard B Hollow porous microspheres as substrates and containers for catalyst
US4303431A (en) 1979-07-20 1981-12-01 Torobin Leonard B Method and apparatus for producing hollow microspheres
US4303730A (en) 1979-07-20 1981-12-01 Torobin Leonard B Hollow microspheres
US4303736A (en) 1979-07-20 1981-12-01 Leonard Torobin Hollow plastic microspheres
US4303732A (en) 1979-07-20 1981-12-01 Torobin Leonard B Hollow microspheres
US4415512A (en) 1979-07-20 1983-11-15 Torobin Leonard B Method and apparatus for producing hollow metal microspheres and microspheroids
US4303731A (en) 1979-08-24 1981-12-01 Torobin Leonard B Compressed gaseous materials in a contained volume
US4421562A (en) 1980-04-13 1983-12-20 Pq Corporation Manufacturing process for hollow microspheres
US4420442A (en) 1981-04-13 1983-12-13 Pq Corporation Manufacturing process for hollow microspheres
US4547468A (en) 1981-08-10 1985-10-15 Terra Tek, Inc. Hollow proppants and a process for their manufacture
US4427068A (en) 1982-02-09 1984-01-24 Kennecott Corporation Sintered spherical pellets containing clay as a major component useful for gas and oil well proppants
US4894285B1 (en) 1982-02-09 1994-01-11 Carbo Ceramics Inc. Sintered spherical pellets containing clay as a major component useful for gas and oil well proppants
US5120455A (en) 1982-10-28 1992-06-09 Carbo Ceramics Inc. Hydraulic fracturing propping agent
US4493875A (en) 1983-12-09 1985-01-15 Minnesota Mining And Manufacturing Company Proppant for well fractures and method of making same
US4680230A (en) 1984-01-18 1987-07-14 Minnesota Mining And Manufacturing Company Particulate ceramic useful as a proppant
US4944905A (en) 1984-01-18 1990-07-31 Minnesota Mining And Manufacturing Company Particulate ceramic useful as a proppant
US4698317A (en) 1984-04-24 1987-10-06 Kanto Kagaku Kabushiki Kaisha Porous cordierite ceramics, a process for producing same and use of the porous cordierite ceramics
US4668645A (en) 1984-07-05 1987-05-26 Arup Khaund Sintered low density gas and oil well proppants from a low cost unblended clay material of selected composition
US4744831A (en) 1984-07-30 1988-05-17 Minnesota Mining And Manufacturing Company Hollow inorganic spheres and methods for making such spheres
US4641709A (en) 1985-05-17 1987-02-10 Conoco Inc. Controlling steam distribution
US4632876A (en) 1985-06-12 1986-12-30 Minnesota Mining And Manufacturing Company Ceramic spheroids having low density and high crush resistance
US4725390A (en) 1985-06-12 1988-02-16 Minnesota Mining And Manufacturing Company Process for making ceramic spheroids
US4639427A (en) 1985-06-28 1987-01-27 Norton Company Stress-corrosion resistant proppant for oil and gas wells
JPS6212646A (ja) 1985-07-09 1987-01-21 宇部興産株式会社 微小無機質発泡体の製造法
US4790688A (en) 1987-01-28 1988-12-13 Eng, Inc. Landfill leachate control process and product
DE3715487A1 (de) 1987-05-09 1988-11-17 Walter Voest Verfahren zur herstellung von bauelementen
US4881951A (en) 1987-05-27 1989-11-21 Minnesota Mining And Manufacturing Co. Abrasive grits formed of ceramic containing oxides of aluminum and rare earth metal, method of making and products made therewith
CA1317978C (en) 1987-06-05 1993-05-18 Thomas E. Wood Microcrystalline alumina-based ceramic articles
DE3724156A1 (de) 1987-07-22 1989-02-02 Norddeutsche Affinerie Verfahren zum herstellen von metallischen oder keramischen hohlkugeln
US4869960A (en) 1987-09-17 1989-09-26 Minnesota Mining And Manufacturing Company Epoxy novolac coated ceramic particulate
US4923714A (en) 1987-09-17 1990-05-08 Minnesota Mining And Manufacturing Company Novolac coated ceramic particulate
BE1002001A4 (fr) 1988-02-18 1990-05-15 Mitsubishi Mining & Cement Co Procede de preparation de microspheres ceramiques.
US4921821A (en) 1988-08-02 1990-05-01 Norton-Alcoa Proppants Lightweight oil and gas well proppants and methods for making and using same
US4921820A (en) 1989-01-17 1990-05-01 Norton-Alcoa Proppants Lightweight proppant for oil and gas wells and methods for making and using same
US4983550A (en) 1988-08-24 1991-01-08 Potters Industries, Inc. Hollow glass spheres
US4964883A (en) 1988-12-12 1990-10-23 Minnesota Mining And Manufacturing Company Ceramic alumina abrasive grains seeded with iron oxide
US4977116A (en) 1989-01-17 1990-12-11 Norton-Alcoa Method for making lightweight proppant for oil and gas wells
DE3907521A1 (de) 1989-03-08 1990-09-13 Albert Kubbutat Verfahren und vorrichtung zur herstellung von leichtbauplatten
JPH02296750A (ja) 1989-05-09 1990-12-07 Agency Of Ind Science & Technol 超微粒中空ガラス球状体の製造方法
US5188175A (en) 1989-08-14 1993-02-23 Carbo Ceramics Inc. Method of fracturing a subterranean formation with a lightweight propping agent
US5240654A (en) 1989-12-22 1993-08-31 Comalco Aluminium Limited Method of making ceramic microspheres
US5219806A (en) 1990-07-16 1993-06-15 Minnesota Mining And Manufacturing Company Alpha phase seeding of transition alumina using chromium oxide-based nucleating agents
DE4022648C2 (de) 1990-07-17 1994-01-27 Nukem Gmbh Verfahren und Vorrichtung zur Herstellung von kugelförmigen Teilchen aus flüssiger Phase
US5133624A (en) 1990-10-25 1992-07-28 Cahill Calvin D Method and apparatus for hydraulic embedment of waste in subterranean formations
DE4042594A1 (de) 1990-11-05 1992-07-02 Nukem Gmbh Verfahren zur herstellung von aluminiumoxidkugeln
DE4115172C2 (de) 1991-05-09 1995-08-24 Nukem Gmbh Verfahren zur Herstellung von Pulver aus stabilisiertem Zirkonoxid und Verwendung des Verfahrens
DE4125133C2 (de) 1991-07-30 1993-09-30 Nukem Gmbh Verfahren und Vorrichtung zur Herstellung von Alginatkugeln
US5282875A (en) 1992-03-18 1994-02-01 Cincinnati Milacron Inc. High density sol-gel alumina-based abrasive vitreous bonded grinding wheel
US5240894A (en) 1992-05-18 1993-08-31 Exxon Chemical Patents Inc. Method for making and using a supported metallocene catalyst system
KR950702608A (ko) 1992-07-28 1995-07-29 테릴 켄트 쿠알리 산화금속으로 피복된 연마 입자, 그것의 제조 방법 및 연마제품(abrasive grain with metal oxide coating, method of making same and abrasive products)
US5213591A (en) 1992-07-28 1993-05-25 Ahmet Celikkaya Abrasive grain, method of making same and abrasive products
CA2102656A1 (en) 1992-12-14 1994-06-15 Dwight D. Erickson Abrasive grain comprising calcium oxide and/or strontium oxide
US5690707A (en) 1992-12-23 1997-11-25 Minnesota Mining & Manufacturing Company Abrasive grain comprising manganese oxide
CA2115889A1 (en) 1993-03-18 1994-09-19 David E. Broberg Coated abrasive article having diluent particles and shaped abrasive particles
US5322821A (en) 1993-08-23 1994-06-21 W. R. Grace & Co.-Conn. Porous ceramic beads
JP2996354B2 (ja) 1993-09-08 1999-12-27 ピー キュー コーポレーション 中空ボロシリケート微小球及び製造方法
EP0739397A1 (en) 1993-12-28 1996-10-30 Minnesota Mining And Manufacturing Company Alpha alumina-based abrasive grain having an as sintered outer surface
BR9408461A (pt) 1993-12-28 1997-08-05 Minnesota Mining & Mfg Tipo nominal especificado de grão abrasivo e artigo abrasivo
MX9504934A (es) 1994-12-12 1997-01-31 Morton Int Inc Revestimientos en polvo de pelicula delgada lisa.
IT1271312B (it) 1994-12-21 1997-05-27 Enirisorse Spa Procedimento sol-gel per ottenere sfere,microsfere o rivestimenti di monoliti a forma cellulare,costituiti da ossido di zirconio puro o misto ad altri ossidi,utili come catalizzatori o supporti per catalizzatori
US5645619A (en) 1995-06-20 1997-07-08 Minnesota Mining And Manufacturing Company Method of making alpha alumina-based abrasive grain containing silica and iron oxide
US6211109B1 (en) 1995-07-18 2001-04-03 Fina Technology, Inc. Process for treating silica with alumoxane
US5669941A (en) 1996-01-05 1997-09-23 Minnesota Mining And Manufacturing Company Coated abrasive article
WO1997030782A1 (fr) 1996-02-20 1997-08-28 Mikuni Corporation Procede de production de materiau granulaire
US5739368A (en) 1996-05-10 1998-04-14 Albemarle Corporation Use of heat treated alumoxanes in preparing supported catalysts
US5728184A (en) 1996-06-26 1998-03-17 Minnesota Mining And Manufacturing Company Method for making ceramic materials from boehmite
US5779743A (en) 1996-09-18 1998-07-14 Minnesota Mining And Manufacturing Company Method for making abrasive grain and abrasive articles
US6206942B1 (en) 1997-01-09 2001-03-27 Minnesota Mining & Manufacturing Company Method for making abrasive grain using impregnation, and abrasive articles
US5893935A (en) 1997-01-09 1999-04-13 Minnesota Mining And Manufacturing Company Method for making abrasive grain using impregnation, and abrasive articles
US6330916B1 (en) 1996-11-27 2001-12-18 Bj Services Company Formation treatment method using deformable particles
US6772838B2 (en) 1996-11-27 2004-08-10 Bj Services Company Lightweight particulate materials and uses therefor
US7426961B2 (en) 2002-09-03 2008-09-23 Bj Services Company Method of treating subterranean formations with porous particulate materials
US20050028979A1 (en) 1996-11-27 2005-02-10 Brannon Harold Dean Methods and compositions of a storable relatively lightweight proppant slurry for hydraulic fracturing and gravel packing applications
US6048470A (en) 1996-12-20 2000-04-11 Asahi Glass Company Ltd. Alumina sol, alumina hydrate powder and processes for their production
US6805737B2 (en) 1997-03-26 2004-10-19 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Lightweight substance molded body, method for the production and use thereof
US7384680B2 (en) 1997-07-21 2008-06-10 Nanogram Corporation Nanoparticle-based power coatings and corresponding structures
US5921317A (en) 1997-08-14 1999-07-13 Halliburton Energy Services, Inc. Coating well proppant with hardenable resin-fiber composites
US5899256A (en) 1997-10-03 1999-05-04 Electric Power Research Institute, Inc. Metal-fly ash composites and low pressure infiltration methods for making the same
US20030180537A1 (en) 1998-01-30 2003-09-25 Black Diamond Granules, Inc. Spheroidal particles and apparatus and process for producing same
US6258456B1 (en) 1998-01-30 2001-07-10 Black Diamond Granules, Inc. Spheroidal slag particles and apparatus and process for producing spheroidal slag and fly ash particles
US6322890B1 (en) 1998-03-30 2001-11-27 Wm. Marsh Rice University Supra-molecular alkylalumoxanes
DK1023382T3 (da) 1998-07-22 2006-06-26 Hexion Specialty Chemicals Inc Sammensat proppant, sammensatte filtreringsmidler og fremgangsmåder til fremstilling og anvendelse deraf
US6582819B2 (en) 1998-07-22 2003-06-24 Borden Chemical, Inc. Low density composite proppant, filtration media, gravel packing media, and sports field media, and methods for making and using same
US6406789B1 (en) 1998-07-22 2002-06-18 Borden Chemical, Inc. Composite proppant, composite filtration media and methods for making and using same
US6369183B1 (en) 1998-08-13 2002-04-09 Wm. Marsh Rice University Methods and materials for fabrication of alumoxane polymers
US6139960A (en) 1999-02-17 2000-10-31 Mineral Resource Technologies, Llc Method of making a mineral filler from fly ash
FR2791580B1 (fr) 1999-04-02 2001-05-04 Centre Nat Rech Scient Procede pour l'enrobage de particules
US6806236B2 (en) 1999-05-13 2004-10-19 Schlumberger Technology Corporation Composition and method for treating a subterranean formation
DK1064990T3 (da) 1999-06-29 2004-05-24 Aeromatic Fielder Ag Fremgangsmåde til granulering af et partikelformet materiale
US6409650B2 (en) 1999-08-25 2002-06-25 Terralog Technologies Usa, Inc. Method for biosolid disposal and methane generation
PL358677A1 (en) 2000-03-14 2004-08-09 James Hardie Research Pty Limited Fiber cement building materials with low density additives
DE10020956B4 (de) 2000-04-28 2005-05-19 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Mauerstein und Verfahren zu seiner Herstellung
DE10020955A1 (de) 2000-04-28 2001-11-22 Fraunhofer Ges Forschung Formkörper und Verfahren zur Herstellung
US6713177B2 (en) 2000-06-21 2004-03-30 Regents Of The University Of Colorado Insulating and functionalizing fine metal-containing particles with conformal ultra-thin films
DE10046298B4 (de) 2000-09-19 2008-11-20 Technum Gmbh Verwendung eines Leichtbauwerkstoffs für den Crash-Schutz
EP1319026A1 (de) 2000-09-21 2003-06-18 MERCK PATENT GmbH Polystyrolmikrokugeln und verfahren zur herstellung
US6372678B1 (en) 2000-09-28 2002-04-16 Fairmount Minerals, Ltd Proppant composition for gas and oil well fracturing
US6528446B1 (en) 2000-10-03 2003-03-04 Kinetico Incorporated Process for making clay spheroids
US6444162B1 (en) 2000-11-27 2002-09-03 The United States Of America As Represented By The United States Department Of Energy Open-cell glass crystalline porous material
US6916891B2 (en) 2001-02-28 2005-07-12 The Standard Oil Company Attrition resistant inorganic microspheroidal particles
US6632528B1 (en) 2001-05-18 2003-10-14 Ensci Inc Metal oxide coated nano substrates
CA2392277C (en) 2001-06-29 2008-02-12 Bj Services Company Canada Bottom hole assembly
US6617285B2 (en) 2001-07-03 2003-09-09 Baker Hughes Incorporated Polyols for breaking of borate crosslinked fracturing fluid
US6753299B2 (en) 2001-11-09 2004-06-22 Badger Mining Corporation Composite silica proppant material
US6962200B2 (en) 2002-01-08 2005-11-08 Halliburton Energy Services, Inc. Methods and compositions for consolidating proppant in subterranean fractures
US7455798B2 (en) 2002-08-23 2008-11-25 James Hardie International Finance B.V. Methods for producing low density products
NZ538497A (en) 2002-08-23 2007-03-30 James Hardie Int Finance Bv Synthetic hollow microspheres
US7972997B2 (en) 2002-09-20 2011-07-05 M-I L.L.C. Process for coating gravel pack sand with polymeric breaker
US7036591B2 (en) 2002-10-10 2006-05-02 Carbo Ceramics Inc. Low density proppant
US7560160B2 (en) 2002-11-25 2009-07-14 Materials Modification, Inc. Multifunctional particulate material, fluid, and composition
US6780804B2 (en) 2003-01-24 2004-08-24 Saint-Gobain Ceramics & Plastics, Inc. Extended particle size distribution ceramic fracturing proppant
WO2005021147A2 (en) 2003-02-06 2005-03-10 William Marsh Rice University High strength polycrystalline ceramic spheres
BR0301036B1 (pt) 2003-04-29 2013-09-10 propante para fraturamento hidráulico de poços de petróleo ou de gás, bem como método para reduzir ou eliminar o fenômeno de reversão de fluxo em poços de petróleo ou de gás
US7036592B2 (en) 2003-05-22 2006-05-02 Halliburton Energy Services, Inc. High strength particles and methods of their use in subterranean operations
US6983797B2 (en) 2003-05-22 2006-01-10 Halliburton Energy Services, Inc. Lightweight high strength particles and methods of their use in wells
US7032664B2 (en) 2004-06-02 2006-04-25 Halliburton Energy Services, Inc. Nanocomposite particulates and methods of using nanocomposite particulates
DE10326252A1 (de) 2003-06-11 2005-01-05 Dennert Poraver Gmbh Verfahren zur Herstellung eines Formkörpers aus einem Leichtzuschlagstoff-Granulat und einem Bindemittel
US20040266933A1 (en) 2003-06-27 2004-12-30 Certainteed Corporation Compositions comprising mineralized ash fillers
US7135231B1 (en) 2003-07-01 2006-11-14 Fairmont Minerals, Ltd. Process for incremental coating of proppants for hydraulic fracturing and proppants produced therefrom
US7066258B2 (en) 2003-07-08 2006-06-27 Halliburton Energy Services, Inc. Reduced-density proppants and methods of using reduced-density proppants to enhance their transport in well bores and fractures
US7871702B2 (en) 2003-07-30 2011-01-18 Halliburton Energy Services, Inc. Particulates comprising silica and alumina, and methods of utilizing these particulates in subterranean applications
US7237609B2 (en) 2003-08-26 2007-07-03 Halliburton Energy Services, Inc. Methods for producing fluids from acidized and consolidated portions of subterranean formations
US20050089631A1 (en) 2003-10-22 2005-04-28 Nguyen Philip D. Methods for reducing particulate density and methods of using reduced-density particulates
CA2447928C (en) 2003-11-04 2007-09-04 Global Synfrac Inc. Proppants and their manufacture
US7244492B2 (en) 2004-03-04 2007-07-17 Fairmount Minerals, Ltd. Soluble fibers for use in resin coated proppant
US20050227874A1 (en) 2004-04-06 2005-10-13 Berger Paul D Composition and method for fracturing subterranean reservoirs
WO2005100007A2 (en) 2004-04-12 2005-10-27 Carbo Ceramics, Inc. Coating and/or treating hydraulic fracturing proppants to improve wettability, proppant lubrication, and/or to reduce damage by fracturing fluids and reservoir fluids
MX2007000072A (es) 2004-07-09 2007-03-27 Carbo Ceramics Inc Metodo para producir particulas ceramicas solidas utilizando un proceso de secado por pulverizacion.
US20060016598A1 (en) 2004-07-21 2006-01-26 Urbanek Thomas W Lightweight proppant and method of making same
WO2006023172A2 (en) 2004-08-16 2006-03-02 Fairmount Minerals, Ltd. Control of particulate flowback in subterranean formations using elastomeric resin coated proppants
CN101023243A (zh) 2004-09-14 2007-08-22 卡博陶粒有限公司 烧结球形颗粒
EP1791691A4 (en) 2004-09-20 2010-06-23 Hexion Specialty Chemicals Res PARTICLES USED AS SUPPORTING AGENTS OR GRAFT GRAPPLES, METHODS OF MAKING AND USING SAME
US7726399B2 (en) 2004-09-30 2010-06-01 Bj Services Company Method of enhancing hydraulic fracturing using ultra lightweight proppants
US20060073980A1 (en) 2004-09-30 2006-04-06 Bj Services Company Well treating composition containing relatively lightweight proppant and acid
US7461696B2 (en) 2004-11-30 2008-12-09 Halliburton Energy Services, Inc. Methods of fracturing using fly ash aggregates
US7322411B2 (en) 2005-01-12 2008-01-29 Bj Services Company Method of stimulating oil and gas wells using deformable proppants
US20060162929A1 (en) 2005-01-26 2006-07-27 Global Synfrac Inc. Lightweight proppant and method of making same
US7867613B2 (en) * 2005-02-04 2011-01-11 Oxane Materials, Inc. Composition and method for making a proppant
US8012533B2 (en) 2005-02-04 2011-09-06 Oxane Materials, Inc. Composition and method for making a proppant
BRPI0606548A2 (pt) 2005-02-04 2009-06-30 Oxane Materials Inc propante, método para produzir um propante, formulação de propante, método para preencher e suportar frações abertas de formações subterráneas e método para tratar uma zona subterránea produtora
AU2006216407A1 (en) 2005-02-24 2006-08-31 James Hardie Technology Limited Alkali resistant glass compositions
BRPI0609373A2 (pt) 2005-03-01 2010-03-30 Carbo Ceramics Inc métodos para produzir partìculas sinterizadas de uma lama de um material bruto contendo alumina
US7528096B2 (en) 2005-05-12 2009-05-05 Bj Services Company Structured composite compositions for treatment of subterranean wells
US20060272816A1 (en) 2005-06-02 2006-12-07 Willberg Dean M Proppants Useful for Prevention of Scale Deposition
US20070023187A1 (en) 2005-07-29 2007-02-01 Carbo Ceramics Inc. Sintered spherical pellets useful for gas and oil well proppants
DE102005045180B4 (de) 2005-09-21 2007-11-15 Center For Abrasives And Refractories Research & Development C.A.R.R.D. Gmbh Kugelförmige Korundkörner auf Basis von geschmolzenem Aluminiumoxid sowie ein Verfahren zu ihrer Herstellung
US7389185B2 (en) 2005-10-07 2008-06-17 Halliburton Energy Services, Inc. Methods and systems for determining reservoir properties of subterranean formations with pre-existing fractures
JP2009512557A (ja) 2005-10-19 2009-03-26 カーボ、サラミクス、インク 低熱膨張鋳造媒体
US20070087941A1 (en) 2005-10-19 2007-04-19 Bj Services Company Storable fracturing suspensions containing ultra lightweight proppants in xanthan based carriers and methods of using the same
US7461697B2 (en) 2005-11-21 2008-12-09 Halliburton Energy Services, Inc. Methods of modifying particulate surfaces to affect acidic sites thereon
CA2573834A1 (en) 2006-01-13 2007-07-13 Diversifield Industries Ltd. Polyurethane proppant particle and use thereof
US20070172654A1 (en) 2006-01-23 2007-07-26 Hexion Specialty Chemicals, Inc. Core for proppant and process for its production
DE102006003295B4 (de) 2006-01-23 2012-07-19 Ibu-Tec Advanced Materials Ag Verwendung eines Kerns für Stützgranulat
US7598209B2 (en) 2006-01-26 2009-10-06 Bj Services Company Porous composites containing hydrocarbon-soluble well treatment agents and methods for using the same
US7494711B2 (en) 2006-03-08 2009-02-24 Bj Services Company Coated plastic beads and methods of using same to treat a wellbore or subterranean formation
RU2006124277A (ru) 2006-07-07 2008-01-20 Шлюмбергер Текнолоджи Б.В. (Nl) Проппант и способ его производства
US7828998B2 (en) 2006-07-11 2010-11-09 Carbo Ceramics, Inc. Material having a controlled microstructure, core-shell macrostructure, and method for its fabrication
EP1884549A1 (en) 2006-08-04 2008-02-06 ILEM Research and Development Establishment Ceramic proppant with low specific weight
EA015865B1 (ru) 2006-08-30 2011-12-30 Карбо Керамикс Инк. Проппант низкой насыпной плотности и способы его изготовления
JP4523021B2 (ja) * 2007-07-18 2010-08-11 建權玻璃開発股▲はん▼有限公司 模様付き結晶化ガラス物品及びその製造方法

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4440866A (en) * 1980-07-07 1984-04-03 A/S Niro Atomizer Process for the production of sintered bauxite spheres
US4654266A (en) * 1985-12-24 1987-03-31 Kachnik Joseph L Durable, high-strength proppant and method for forming same
US20070166541A1 (en) * 2005-02-04 2007-07-19 Smith Russell J Composition and method for making a proppant

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP2516152A4 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105452193A (zh) * 2013-08-07 2016-03-30 哈利伯顿能源服务公司 支撑剂及其制备方法
CN105452193B (zh) * 2013-08-07 2018-04-13 哈利伯顿能源服务公司 支撑剂及其制备方法

Also Published As

Publication number Publication date
CA2785366A1 (en) 2011-06-30
EP2516152A4 (en) 2013-07-03
US8178476B2 (en) 2012-05-15
EP2516152A1 (en) 2012-10-31
AR081515A1 (es) 2012-10-03
CN102781663B (zh) 2016-04-06
AU2010333894B2 (en) 2014-03-13
US20110146985A1 (en) 2011-06-23
EA201290543A1 (ru) 2013-01-30
CN102781663A (zh) 2012-11-14
KR20120105536A (ko) 2012-09-25
IN2012DN05062A (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html) 2015-10-09
BR112012015322A2 (pt) 2019-09-24
AU2010333894A1 (en) 2012-07-12
MX2012007248A (es) 2012-07-30
MY162476A (en) 2017-06-15
CA2785366C (en) 2018-07-17

Similar Documents

Publication Publication Date Title
US8178476B2 (en) Proppant having a glass-ceramic material
AU2013296818B2 (en) Synthetic proppants and monodispersed proppants and methods of making the same
US9315719B2 (en) Low surface friction proppants
US9796915B2 (en) Light weight proppant with improved strength and methods of making same
US10161236B2 (en) Methods for fracturing subterranean formations
US10233386B2 (en) Light weight proppant with improved strength and methods of making same
US10000690B2 (en) Ceramic particles with controlled pore and/or microsphere placement and/or size and method of making same
HK1176037A (en) A proppant having a glass-ceramic material

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 201080064478.0

Country of ref document: CN

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 10839988

Country of ref document: EP

Kind code of ref document: A1

WWE Wipo information: entry into national phase

Ref document number: 5062/DELNP/2012

Country of ref document: IN

REEP Request for entry into the european phase

Ref document number: 2010839988

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: 2010839988

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: 2010333894

Country of ref document: AU

Ref document number: MX/A/2012/007248

Country of ref document: MX

NENP Non-entry into the national phase

Ref country code: DE

ENP Entry into the national phase

Ref document number: 2785366

Country of ref document: CA

ENP Entry into the national phase

Ref document number: 2010333894

Country of ref document: AU

Date of ref document: 20101213

Kind code of ref document: A

WWE Wipo information: entry into national phase

Ref document number: 201290543

Country of ref document: EA

ENP Entry into the national phase

Ref document number: 20127019149

Country of ref document: KR

Kind code of ref document: A

REG Reference to national code

Ref country code: BR

Ref legal event code: B01A

Ref document number: 112012015322

Country of ref document: BR

ENP Entry into the national phase

Ref document number: 112012015322

Country of ref document: BR

Kind code of ref document: A2

Effective date: 20120621