WO2005104683A2 - Colloidal compositions and methods of preparing same - Google Patents
Colloidal compositions and methods of preparing same Download PDFInfo
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- WO2005104683A2 WO2005104683A2 PCT/US2005/012371 US2005012371W WO2005104683A2 WO 2005104683 A2 WO2005104683 A2 WO 2005104683A2 US 2005012371 W US2005012371 W US 2005012371W WO 2005104683 A2 WO2005104683 A2 WO 2005104683A2
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
- C01B33/14—Colloidal silica, e.g. dispersions, gels, sols
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/02—Cosmetics or similar toiletry preparations characterised by special physical form
- A61K8/04—Dispersions; Emulsions
- A61K8/042—Gels
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/19—Cosmetics or similar toiletry preparations characterised by the composition containing inorganic ingredients
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/19—Cosmetics or similar toiletry preparations characterised by the composition containing inorganic ingredients
- A61K8/25—Silicon; Compounds thereof
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/30—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
- A61K8/40—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing nitrogen
- A61K8/41—Amines
- A61K8/416—Quaternary ammonium compounds
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q19/00—Preparations for care of the skin
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/0004—Preparation of sols
- B01J13/0008—Sols of inorganic materials in water
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
- C01B33/14—Colloidal silica, e.g. dispersions, gels, sols
- C01B33/141—Preparation of hydrosols or aqueous dispersions
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
- C01B33/26—Aluminium-containing silicates, i.e. silico-aluminates
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B37/00—Compounds having molecular sieve properties but not having base-exchange properties
- C01B37/02—Crystalline silica-polymorphs, e.g. silicalites dealuminated aluminosilicate zeolites
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
- C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K2800/00—Properties of cosmetic compositions or active ingredients thereof or formulation aids used therein and process related aspects
- A61K2800/10—General cosmetic use
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/60—Particles characterised by their size
- C01P2004/62—Submicrometer sized, i.e. from 0.1-1 micrometer
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/60—Particles characterised by their size
- C01P2004/64—Nanometer sized, i.e. from 1-100 nanometer
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/12—Surface area
Definitions
- the present invention generally relates to colloidal compositions and methods of producing same. More specifically, the present invention relates to colloidal silicas, such as silicas that have a metal dispersed therein over a wide range of metal content and that can be dispersed in a controlled manner.
- colloidal materials such as colloidal silica
- colloidal silica with a metal-coated surface is generally known and used.
- the silica colloid is first synthesized.
- the colloid is then coated with a metal oxide.
- metal containing silica colloids are useful in a multitude of applications, such as chemical mechanical polishing agents in the electronics industry, specialty coating applications, and as support materials in catalytic processes.
- conventional-type silica colloids have several disadvantages.
- the amount and type of metal component to be added to the silica particle is effectively limited to the surface area and surface morphology of the particle.
- conventional surface-treated silica sols are unstable at neutral pH, i.e., pH 6-8.
- aluminosilicate colloids for example, aluminum species unbound or weakly bound to the colloidal particle surface typically hydrolyze under neutral pH conditions. This can result in either precipitation or coagulation of the particle coating material. This is particularly problematic for the electronics industry as the demand continues to rise for chemical mechanical polishing slurries that are stable at neutral pH.
- the present invention generally relates to colloidal compositions and methods of producing same.
- the present invention relates to colloidal compositions that include a silicate with a metal dispersed within the silicate and at varying metal loadings that can range from as high as about 35 wt% based on silica.
- the colloidal compositions can further include a stabilizer, such as a quaternary compound, that can facilitate the dispersion and loading of the metal within the silicate.
- the present invention provides a novel and unique alternative to conventional surface-treated silica colloids.
- the colloidal compositions of the present invention can be made in any suitable way.
- the colloidal compositions are, in general, synthesized according to two procedures as further detailed below pursuant to various embodiments of the present invention.
- a method of producing a silica colloid includes providing an alkaline solution having a stabilizing component, adding a silicic acid solution to the alkaline solution, and forming a colloid of silica particles wherein the stabilizing component is dispersed throughout each particle.
- a cationic metal component can be added to the stabilizer-containing alkaline solution in an embodiment.
- the stabilizer is a quaternary compound, preferably a quaternary amine, such as a quaternary ammonium hydroxide and the like.
- the stabilizer performs several functions in the synthesis of the colloidal silica. For example, the stabilizer provides the OH " component to the alkaline solution, which catalyzes the reaction between the silicic acid and metal component to form the colloid.
- the stabilizer also enables more of the metal component to bond or chemically combine with the silica component during formation of the colloid.
- the resultant silica colloid demonstrates the capability to carry increased amounts of metal.
- the colloid can have a metal content from about .0001wt% to about 35wt% based on silica.
- the colloidal particles are amorphous and spherical in shape.
- the colloidal composition can be further processed to produce a crystalline structure as described in greater detail below.
- the diameter of the colloidal particles is in the range of about 2 nm to about 1000 run according to an embodiment.
- a method of preparing a metal- containing silica colloid wherein a silicic acid solution is reacted with a cationic metal component to form a metal silicate solution.
- the metal silicate solution is subsequently added to an alkaline solution to form a colloid of metal silicate particles.
- Reacting the silicic acid solution with the metal component forms a metal- silicate monomer that is subsequently polymerized as the metal silicate solution is added to the alkaline solution.
- the polymerization forms a homogeneous metal- silicate lattice microstructure or framework throughout the entire solid phase of the colloid.
- the polymerization of the metal-silicate and the utilization of a polyvalent cationic metal component in formation of the colloid yields a metal silicate colloids having metal content in the range of about .0001% to as high as 2% by weight silica according to an embodiment.
- the lattice metal-silicate structure throughout the entire solid phase also improves the stability of the colloid.
- the metal silicate colloid of the present invention remains soluble throughout the entire pH range, i.e., pH 1-14.
- the solid phase of the metal silicate colloid of the present invention is substantially amorphous having a generally spherical particle shape and size in the range of from about 2 nm to about 1000 nm according to an embodiment.
- the location of a metal component within the metal-containing silica colloid can be effectively controlled.
- the metal silicate solution and the silicic acid solution can be selectively added to the alkaline solution to form a colloid of silica particles containing metal that is dispersed within one or more of the particles.
- the sequence and duration in which the metal silicate solution and the silicic acid solution are added effectively controls the location of the metal within the solid phase of the colloid.
- the metal silicate solution can be added to the alkaline solution before the silicic acid solution to form a colloid of silica particles having metal dispersed within an interior core layer of each particle.
- the silicic acid solution can be added to the alkaline solution before the metal silicate solution to form a colloid of silica particles having a silica core and metal dispersed within an outer or exterior layer of each particle.
- the metal silicate solution and the silicic acid solution can be added to the alkaline solution in an alternating manner to form a colloid of silica particles having a number of layers, wherein the layers alternate between metal containing layers and layers containing only silica in a repeat or successive manner.
- the present invention provides a colloidal composition.
- the colloidal composition includes a silicate doped with a metal, and a stabilizer dispersed within the silicate.
- the silicate doped with metal includes about 35 wt % or less of metal based on silica.
- the stabilizer includes a quaternary compound.
- the quaternary compound is a quaternary amine.
- an amount of the stabilizer correlates to an amount of the metal.
- the present invention provides a colloidal silicate composition doped with a metal.
- the colloidal silicate composition includes one or more silicate particles wherein the metal is dispersed within one or more of the silicate particles.
- the metal is dispersed in a controlled manner.
- one or more of the silicate particles includes a layered structure.
- the metal is controllably dispersed within one or more particle layers of the layered structure.
- the metal includes an alkali metal, an alkaline earth metal, a 1 st row transition metal, a 2 nd row transition metal, a lanthanide, and combinations thereof.
- the metal is about 2 wt % or less based on silica.
- the present invention provides a method of forming a colloidal composition. The method includes preparing a heel solution including a stabilizer; preparing a silicic acid solution; and mixing and further processing the heel solution and the silicic acid solution to form the colloidal composition.
- a metal is added to the heel solution.
- the colloidal composition includes the stabilizer and a silicate doped with the metal such that the stabilizer and the metal are dispersed within one or more particles of the silicate.
- the metal includes about 35 wt % or less based on silica.
- the colloidal composition is further processed to form a crystalline structure.
- the colloidal composition is further processed by heating.
- a metal is added to the heel solution prior to crystallization.
- the colloidal composition includes a zeolite.
- the stabilizer includes a quaternary amine.
- the present invention provides a method of forming a colloidal silicate composition.
- the method includes preparing a silicic acid solution, a metal silicate solution and an alkaline solution; mixing and further processing the silicic acid solution and the metal silicate solution with the alkaline solution; and forming one or more silicate particles doped with a metal wherein the metal is dispersed within one or more of the silicate particles.
- the metal is dispersed in a controlled manner.
- the silica doped with metal includes about 2 wt % or less of the metal based on silica.
- the metal includes an alkali metal, an alkaline earth metal, a
- a method of controlling a location of a metal within a metal-containing silica colloid includes preparing a silicic acid solution, a metal silicate solution and an alkaline solution; and selectively adding the metal silicate solution and the silicic acid solution to the alkaline solution to form a colloid of silica particles containing the metal.
- the method further comprises adding the metal silicate solution before the silicic acid solution and forming the colloid of silica particles having the metal dispersed within an interior layer of one or more of the silica particles.
- the method further comprises adding the silicic acid solution before the metal silicate solution and forming the colloid of silica particles having the metal dispersed within an outer layer of one or more of the silica particles.
- the method further comprises adding the metal silicate solution and the silicic acid solution in an alternating manner and forming the colloid of silica particles having a metal-containing layer and a non-metal containing layer.
- of the silica particles includes a layered structure that has the non-metal containing layer disposed on the metal containing layer in a repeat manner. Additional features and advantages of the present invention are described in and will be apparent from the following Detailed Description of the Presently Preferred Embodiments.
- the present invention generally relates to colloidal compositions and methods of preparing same.
- colloidal and other like terms including “colloidal”, “sol”, and the like refer to a two-phase system having a dispersed phase and a continuous phase.
- the colloids of the present invention have a solid phase dispersed or suspended in a continuous or substantially continuous liquid phase, typically an aqueous solution.
- the term “colloid” encompasses both phases whereas “colloidal particles” or “particles” refers to the dispersed or solid phase.
- the present invention relates to colloidal compositions that include a silicate and that can be made in a readily and cost effective manner as described below in greater detail.
- the present invention provides two types of synthesis procedures.
- the present invention utilizes a heel solution that includes a stabilizer, such as a quaternary compound.
- the stabilizer can enhance the colloidal synthesis in a number of ways, such as by stabilizing and better enabling a metal to be dispersed within the silicate of the colloidal composition. It is believed that the stabilizer can also enhance the ability of the silicate to have higher metal loading, such as about 35wt% or less based on silica.
- silicic acid and a metal silicate solution are selectively added to an alkaline solution thereby producing a colloid that includes a silicate with a metal dispersed therein in a controlled manner.
- a method of preparing a colloidal composition provides adding a silicic acid solution to a reaction vessel that includes a heel solution having an aqueous solution containing a metal component and a stabilizing component to form a colloid of silica particles.
- the stabilizer is an amine or quaternary compound.
- Nonlimiting examples of amines suitable for use as the stabilizer include dipropylamine, trimethylamine, triethylmine, tri-n-propylamine, diethanolamine, monoethanolamine, triethanolamine, diisobutylamine, isopropylamine, diisopropylamine, dimethylamine, ethylenediaminetetraacetic acid, pyridine, the like and combinations thereof.
- the stabilizing component is a quaternary amine that forms an alkaline solution when dispersed in water, such as quaternary ammonium hydroxides.
- the quaternary amine includes a tetraalkyl ammonium ion wherein each alkyl group has a carbon chain length of 1 to 10, the alkyl groups being the same or different.
- quaternary amines suitable for use as the stabilizer include tetramethylammonium hydroxide (TMAOH), tetrapropylammonium hydroxide (TPAOH), tetraethylammonium hydroxide (TEAOH), ' tetrabutylammonium hydroxide (TBAOH), tetrahexylammonium hydroxide, tetraoctylammonium hydroxide, tributylmethylammonium hydroxide, triethylmethylammonium hydroxide, trimethylphenylammonium hydroxide, methyltripropylammonium hydroxide, dodecyltrimethylammonium hydroxide, hexadecyl
- the bromide and chloride forms of the above mentioned ammonium salts can be used by passing through a hydroxide (anion)-exchange column to produce the alkylammonium hydroxide materials.
- the metal can include any suitable material and be derived from any suitable material including metal salts that are soluble or substantially soluble in an aqueous solution.
- the metal includes an alkali metal, an alkaline earth metal, a 1 st row transition metal, a 2 nd row transition metal, a lanthanide, and combinations thereof.
- Preferred metal components include aluminum, cerium, titanium, tin, zirconium, zinc, copper, nickel, molybdenum, iron, rhenium, vanadium, boron, the like and any combination thereof.
- the silicic acid solution can be prepared by passing a sodium silicate solution through a bed of HXation exchange resin.
- the resulting deionized silicic acid solution tends to be quite reactive and is typically kept cooled to retard polymerization.
- the disassociated OH " from the stabilizer catalyzes a polymerization reaction between the cationic metal component and a silicate component from the silicic acid to form the colloid of silica particles.
- the reaction thereby yields a solid phase composed of the metal component, the stabilizer and silica wherein the metal and stabilizer are dispersed within the silica particles.
- the stabilizer component obviates the need to provide a heel containing alkaline catalysts, such as NaOH, KOH, NH OH, the like, and combinations thereof. It should be appreciated that any suitable type of silicic acid solution can be utilized.
- the stabilizer serves as a stabilizing agent for the metal component. Not wishing to be bound to any particular theory, it is believed that the quaternary amine cation interacts with the metal oxide anion in the heel (M0 4 x" wherein M is the metal cation) ultimately stabilizing the metal.
- the quaternary amine maintains the metal oxide anion in a four-fold coordination state or tetrahedral orientation so that silicon-to-metal ratios of four can be obtained. Stabilizing the metal component in this manner produces a greater number of silicon-metal linkages allowing the solid phase of the colloid to carry an increased amount of metal compared to surface treated colloids, for example.
- the resultant silica colloid is capable of supporting from about 0.000 lwt% to about 35wt% metal based on silica.
- the metal-stabilized silica solid phase also demonstrates increased stability and remains stable in a pH range of about 1 to about 14.
- stable means that the solid phase of the colloid is present, dispersed through the medium and stable throughout this entire pH range with effectively no precipitate.
- the solid phase in an embodiment is amorphous and has a number of particles that are generally spherical in shape.
- the colloidal particles have a diameter in the range of about 2 nanometers (nm) to about 1000 nm pursuant to an embodiment.
- silicic acid is utilized to incorporate or disperse a metal component into the framework of colloidal silica (i.e., doping).
- the method includes preparing a heel.
- the heel includes an aqueous solution that at least includes a quaternary amine as defined herein or an alkaline agent.
- Suitable alkaline agents include, for example, NaOH, KOH, NH OH, the like and combination thereof.
- the silicic acid solution (can be prepared as previously discussed or other suitable manner) is reacted with a cationic metal component to form a metal silicate solution, represented chemically below: H 4 Si0 4 + M x+ ⁇ [x(H 3 Si ⁇ ;) - M x+ ] + xH +
- the metal silicate solution is subsequently added to the heel to form the colloid.
- the OH " present in the heel catalyzes the copolymerization of the cationic metal component and silicate (Si0 4 " ) from the silicic acid.
- Nonlimiting examples of suitable metals that can be used as the cationic metal component include aluminum, cerium, titanium, tin, zirconium, zinc, copper, nickel, molybdenum, iron, rhenium, vanadium, boron, 1 st and 2 nd row transition metals, lanthanides, alkali metals, alkaline earth metals, the like and any combination thereof.
- the metal component can be derived from any suitable metal source including, for example, any suitable metal salt that is soluble or substantially soluble in an aqueous solution.
- metal silicate colloids of the present invention can have a metal content from about 0.0001% to about 2% by weight based on silica.
- the metal silicate colloids of the present invention are amorphous and generally spherical in shape, wherein the particles have an effective diameter or particle size from about 2 nm to about 1000 nm in an embodiment.
- the metal silicate colloids are stable at a pH range from about 1 to about 14, exhibiting effectively no precipitation in this range.
- the size of the colloidal particles can be adjusted by varying the addition time of the metal silicate solution to the heel. As previously discussed, the above-described synthesis procedure can be utilized to effectively control the location of the method and loading thereof within the colloidal particles.
- the metal silicate solution and the silicic acid solution are selectively added to the heel to control the position of the metal within the solid phase of the colloid as desired.
- Both silicic acid solution and metal silicate solution can be added to the heel to initiate particle formation or to grow or otherwise increase the size of a pure silica particle initially added to the heel.
- the metal silicate solution is added to the heel before the silicic acid solution in an embodiment.
- This addition sequence yields a metal containing silica colloid wherein the metal is dispersed in a core or interior layer of the colloidal particle.
- the subsequent addition of the silicic acid can be used to cover the interior metal- containing portion of the particle with a layer containing on silica without the metal.
- the silicic acid solution can be added to the heel prior to the addition of the metal silicate solution in an embodiment.
- This addition sequence yields colloidal particles having a core or interior composed of silica.
- the metal silicate solution can then be added to coat the silica particle to produce a particle containing metal on an exterior surface or outer layer of the particle wherein the metal is dispersed within this particle layer.
- the skilled artisan will appreciate the myriad of possibilities available for the composition of the colloid solid phase. Addition of only the metal silicate solution to the heel can yield a colloid having a dispersion or distribution of metal within one or more of the colloidal particle as previously discussed. Adding the metal silicate solution and the silicic acid solution in an alternating manner or a sequence such as metal silicate-silicic acid-metal silicate-silicic acid can yield a colloidal particle having a number of layers wherein metal containing layers are separated by layers containing silica and without a metal in an embodiment.
- the duration of silicic acid and/or metal silicate addition can be varied as desired to vary the width or thickness of each particle layer in the colloid.
- the multiple layered colloid particles of the present invention are generally spherical in shape and have an effective particle size of about 2 nm to about 1000 nm according to an embodiment.
- the colloidal compositions and methods of making same can be modified in any suitable manner.
- the colloidal compositions as described above can be further processed to form a crystalline structure, such as a crystalline silicate, a crystalline metallosilicate including a zeolite, the like and combinations thereof.
- continued hydrothermal treatment at suitable temperatures and over a suitable period of time can produce a more crystalline silicate including metallosilicates, such as zeolites, from the colloidal compositions described- above wherein the colloidal composition includes silicate and a stabilizer with or without a metal dispersed within the silicate, specific examples of which are provided below in greater detail.
- metallosilicates such as zeolites
- a stabilizer including tetramethylammonium hydroxide (TMAOH), tetrapropylammonium hydroxide (TPAOH), tetraethylammonium hydroxide (TEAOH) and/or the like e.g., a stabilizer including tetramethylammonium hydroxide (TMAOH), tetrapropylammonium hydroxide (TPAOH), tetraethylammonium hydroxide (TEAOH) and/or the like
- TMAOH tetramethylammonium hydroxide
- TPAOH tetrapropylammonium hydroxide
- TEAOH tetraethylammonium hydroxide
- Doped colloidal silica is useful in multitudinous industrial applications including, for example, dental applications, protein separation, molecular sieves, nanoporous membranes, wave guides, photonic crystals, refractory applications, clarification of wine and juice, chemical mechanical planarization of semiconductor and disk drive components, catalyst supports, retention and drainage aids in papermaking, fillers, surface coatings, ceramic materials, investment casting binders, flattening agents, proppants, cosmetic formulations, particularly sunscreens, and polishing abrasives in the glass, optical and electronics and semiconductor industries.
- the form of silica used in a particular application depends in large part on the silica particle's size and porosity characteristics. Doped colloidal silica having the desired characteristics is readily prepared according to the method of this invention.
- this invention is a material for use in an industrial application comprising the colloidal composition described herein.
- the industrial application is selected from the group consisting of catalyst supports, retention and drainage aids in papermaking, fillers, flattening agents, proppants and polishing abrasives.
- Polyvalent aluminum containing solution A second solution of 0.50 M A1C1 3 -6H 2 0 was prepared. This solution was passed through an ion exchange column containing an anion exchange resin (Dowex
- silicic acid 25.00 g of (sodium silicate) was added to 57.37 g of Dl water. The solution was passed through a column containing a cation exchange resin (Dowex 650C (H + )). About 40 mL of resin for 100 g of diluted sodium silicate solution was used to produce a silicic acid solution. To the silicic acid solution, a suitable amount of aluminum containing solution to produce the desired concentration (ppm) of aluminum based on silica (BOS) was added as detailed below in Table 2. 3.
- ppm aluminum containing solution to produce the desired concentration (ppm) of aluminum based on silica
- Example 1 The silicic acid solution/monomeric aluminum solution (2.93 g of 0.37 M A1C1 3 -6H 2 0 solution) was added to a caustic heel containing 0.30 g of NaOH (50 wt%) in 14.40 g of Dl water over a 5.0 hours ramp. A total of 68.57 g of silicic acid solution/aluminum solution was added.
- Example 2 The silicic acid solution/polyvalent aluminum solution (3.02 g of 0.50 M A1C1 3 -6H 2 0 anion-exchanged solution) was added to a caustic heel containing 0.30 g of NaOH (50 wt%) in 14.20 g of Dl water over a 5.0 hour ramp. A total of 68.57 g of silicic acid solution/aluminum solution was added.
- Example 3 The silicic acid solution/polyvalent aluminum solution (3.02 g of
- Example 4 The silicic acid solution/aluminum solution (3.02 g of 0.50 M A1C1 -6H 2 0 anion-exchanged solution) was added to a caustic heel containing 0.30 g of NaOH (50 wt%) in 14.20 g of Example 3 over a 5.0 hour ramp. A total of 68.57 g of silicic acid solution/aluminum solution was added.
- Example 4 The silicic acid solution/aluminum solution (3.02 g of 0.50 M A1C1 -6H 2 0 anion-exchanged solution) was added to a caustic heel containing 0.30 g of NaOH (50 wt%) in 14.20 g of Example 3 over a 5.0 hour ramp. A total of 68.57 g of silicic acid solution/aluminum solution was added.
- Example 5 Pilot Plant synthesis: The silicic acid solution/aluminum solution (0.67 g of a 0.87 M solution of aluminum chlorohydrate) was added to a caustic heel containing 0.11 g NaOH (50 wt%) in 3.82 g of 20 nm silica sol in 8.18 g of Dl water over a 4.75 hours ramp. The reaction was heated at 93°C. A total of 87.89 g of silicic acid solution/aluminum solution was added. The final product was cation-exchanged to remove excess sodium, large particle filtered (LPC) and pH adjusted to 6.4.
- LPC large particle filtered
- Example 6 Cerium doped silica colloids: A solution of 0.50 M Ce 2 (C0 3 ) was prepared by adding 46g Ce 2 (C0 3 ) into 100ml Dl water then adding IN HC1 until dissolved. The solution was then topped up to 200ml with Dl water. A silicic acid solution was prepared where 200 g of (sodium silicate) was added to 1000 g of Dl water. The solution was passed through a column containing a cation exchange resin (Dowex 650C (H*)). About 40 mL of resin for 100 g of diluted sodium silicate solution was used.
- a cation exchange resin Dowex 650C (H*)
- a titanium containing solution was prepared.
- a solution of 0.50 M TiCl 4 was prepared by slowly adding 100ml Dl water into a beaker containing 9.4g TiC14 and 10ml isopropyl alcohol .
- the silicic acid was prepared in the same fashion as described in Example 6. To the silicic acid was added an amount of the titanium containing solution to produce the desired concentration (ppm) of titanium based on silica (BOS) as illustrated below in Table 2.
- the silicic acid solution/titanium solution (12.6 ml of 0.5 M TiC14 solution) was added to a caustic heel containing 5 g of KOH (45 wt%) in 200 g of Dl water over a 5.0 hours ramp.
- Example 8 Zinc doped silica colloids: The zinc containing solution used in this procedure was a commercially- available product, namely IN Zn(N0 3 ) 2 .
- the silicic acid was prepared in the same fashion as described in Example 6. To the silicic acid was added an amount of zinc containing solution to provide the desired concentration (ppm) of zinc based on silica (BOS) as illustrated below in Table 2.
- Example 9 Colloidal Silicalite-1 was synthesized with a narrow particle size distribution from a mole composition of: lTPAOH:1.9SiO 2 :109H 2 O
- the source of silica was silicic acid.
- the reactor vessel was charged with a 20-25 wt% solution of TPAOH, which was heated to 90°C. To this, the silicic acid was added over 3 hours. A clear solution resulted, which was heated for 18 hours.
- Example 10 Colloidal ZSM-5 was synthesized with a narrow particle size distribution from a mole composition of: 65TPAOH:125SiO 2 :lAl 2 O 3 :7000H 2 O
- the source of silica was silicic acid.
- the reactor vessel was charged with a 20-25 wt% solution of TPAOH, which was heated to 90°C. To this the aluminum/silicic acid solution was added over 2 hours. A clear solution resulted, which was heated for 24 hours. *
- Metallosilicate colloids Table 2 shows the various prepared metal doped samples with the different heels, pH of the different metal containing solutions, amounts of metal added to the acid sol based on silica (BOS) and a variety of characterization techniques to determine particle size and the extent, if any, agglomeration. As shown below, Table 2 provides a summary of the synthesis procedures according to Examples 1-10 as detailed above:
- 'Aluminum source is anion exchanged to remove chloride and increase pH.
- BOS means based on silica. Example 5 after cation deionization and pH adjusted to 6.87.
- the metal doped colloids described above and made pursuant to various embodiments exhibit good stability in the pH range 3-9.
- a stability test was conducted on the filtered and cation deionized aluminosilicate colloid of Example 5. The pH was adjusted to 4.1, 6.5 and 8.5 and effective particle diameters were measured (QELS) before and after heat treatment for two weeks at 60°C. No gelation occurred with these samples after heat treatment and the particle diameters remained essentially the same as demonstrated below in Table 3:
- colloidal compositions of the present invention can be utilized in a number of different and suitable types of applications in any suitable forms and amounts thereof.
- the colloidal composition can be used as a chemical mechanical polishing agent including use for electronic components; a catalyst material and supports thereof including use in the petrochemical industry, such as cracking to increase fractions of gasoline; as a detergent or agent thereof to remove calcium ions and/or the like from solution; and any other types of suitable applications.
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Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2007509513A JP5103168B2 (ja) | 2004-04-19 | 2005-04-13 | コロイド状組成物およびその調製方法 |
| EP05735668.5A EP1744825B1 (en) | 2004-04-19 | 2005-04-13 | Colloidal compositions and methods of preparing same |
| BRPI0509859-9A BRPI0509859B1 (pt) | 2004-04-19 | 2005-04-13 | Método para controlar uma localização de um metal dentro de um colóide de sílica contendo metal |
| CN2005800118801A CN1942237B (zh) | 2004-04-19 | 2005-04-13 | 胶体组合物及其制备方法 |
| CA2560748A CA2560748C (en) | 2004-04-19 | 2005-04-13 | Colloidal compositions and methods of preparing same |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US10/827,214 US20050234136A1 (en) | 2004-04-19 | 2004-04-19 | Colloidal compositions and methods of preparing same |
| US10/827,214 | 2004-04-19 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2005104683A2 true WO2005104683A2 (en) | 2005-11-10 |
| WO2005104683A3 WO2005104683A3 (en) | 2006-11-30 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2005/012371 Ceased WO2005104683A2 (en) | 2004-04-19 | 2005-04-13 | Colloidal compositions and methods of preparing same |
Country Status (10)
| Country | Link |
|---|---|
| US (2) | US20050234136A1 (enExample) |
| EP (1) | EP1744825B1 (enExample) |
| JP (1) | JP5103168B2 (enExample) |
| KR (1) | KR20070027535A (enExample) |
| CN (2) | CN1942237B (enExample) |
| BR (1) | BRPI0509859B1 (enExample) |
| CA (1) | CA2560748C (enExample) |
| SG (1) | SG152248A1 (enExample) |
| TW (1) | TWI377980B (enExample) |
| WO (1) | WO2005104683A2 (enExample) |
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| JP2009018960A (ja) * | 2006-04-04 | 2009-01-29 | Nalco Co | ポリシリケート粒子状材料の製造および使用 |
| JP2010509496A (ja) * | 2006-11-08 | 2010-03-25 | ナルコ カンパニー | 高金属性ケイ質組成物及び同一物を生成する方法 |
| CN102344761A (zh) * | 2011-08-03 | 2012-02-08 | 南通海迅天恒纳米科技有限公司 | 一种铈掺杂二氧化硅溶胶的制备方法 |
| WO2013028958A1 (en) | 2011-08-25 | 2013-02-28 | Basf Corporation | Molecular sieve precursors and synthesis of molecular sieves |
| CN101225282B (zh) * | 2007-01-19 | 2013-05-01 | 安集微电子(上海)有限公司 | 一种低介电材料抛光液 |
| US10087081B2 (en) | 2013-03-08 | 2018-10-02 | Ecolab Usa Inc. | Process for producing high solids colloidal silica |
| EP3368478A4 (en) * | 2015-10-26 | 2019-06-05 | Ecolab USA Inc. | VERY HOMOGENEOUS ZEOLITE PRELUDE |
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| US8052788B2 (en) * | 2005-08-10 | 2011-11-08 | Nalco Company | Method of producing silica sols with controllable broad size distribution and minimum particle size |
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2913419A (en) | 1956-04-18 | 1959-11-17 | Du Pont | Chemical process and composition |
| US2974108A (en) | 1957-01-14 | 1961-03-07 | Du Pont | Aluminosilicate aquasols and their preparation |
Family Cites Families (33)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1552341A (en) * | 1921-09-13 | 1925-09-01 | L D Caulk Company | Dental cement and process of making same |
| US2736668A (en) * | 1952-05-09 | 1956-02-28 | Du Pont | Process of methoxylating the surface of a siliceous material, and the resulting product |
| US4243828A (en) * | 1963-02-27 | 1981-01-06 | Mobil Oil Corporation | Alkylation of aromatics using a high silica zeolite |
| US3442795A (en) * | 1963-02-27 | 1969-05-06 | Mobil Oil Corp | Method for preparing highly siliceous zeolite-type materials and materials resulting therefrom |
| US4287086A (en) * | 1975-05-02 | 1981-09-01 | Nl Industries, Inc. | Viscous organic systems containing an organophilic clay gellant without an organic dispersant therefor |
| GR66589B (enExample) * | 1978-06-22 | 1981-03-30 | Snam Progetti | |
| IT1127311B (it) * | 1979-12-21 | 1986-05-21 | Anic Spa | Materiale sintetico,cristallino,poroso costituito da ossidi di silicio e titanio,metodo per la sua preparazione e suoi usi |
| US4468023A (en) * | 1981-10-13 | 1984-08-28 | Solloway Daniel S | Aquatic neck exercise assembly |
| DE3370150D1 (en) | 1982-11-10 | 1987-04-16 | Montedipe Spa | Process for the conversion of linear butenes to propylene |
| US4623142A (en) * | 1984-01-31 | 1986-11-18 | Mackechnie Bruce | Hand held, multi-directional device for aquatic exercising |
| US4670617A (en) * | 1985-12-30 | 1987-06-02 | Amoco Corporation | Propylation of toluene with a high surface area, zinc-modified, crystalline silica molecular sieve |
| NO300125B1 (no) | 1988-03-16 | 1997-04-14 | Nissan Chemical Ind Ltd | Stabil væskeformig silikasol, samt fremgangsmåte ved fremstilling derav |
| JP2803134B2 (ja) * | 1988-03-16 | 1998-09-24 | 日産化学工業株式会社 | 細長い形状のシリカゾル及びその製造法 |
| US5221497A (en) * | 1988-03-16 | 1993-06-22 | Nissan Chemical Industries, Ltd. | Elongated-shaped silica sol and method for preparing the same |
| US5031904A (en) * | 1988-06-20 | 1991-07-16 | Solloway Daniel S | Aquatic boot |
| EP0512986A4 (en) * | 1990-01-31 | 1993-04-07 | Industrial Progress, Inc. | Functional complex microgels with rapid formation kinetics |
| US5024826A (en) * | 1990-03-05 | 1991-06-18 | E. I. Du Pont De Nemours And Company | Silica particulate composition |
| DE4211050C2 (de) | 1992-04-02 | 1995-10-19 | Siemens Ag | Verfahren zur Herstellung eines Bipolartransistors in einem Substrat |
| FI952954A0 (fi) * | 1992-12-16 | 1995-06-15 | Chevron Res & Tech | Alumosilikaattizeoliittien valmistus |
| JP3517913B2 (ja) * | 1993-10-15 | 2004-04-12 | 日産化学工業株式会社 | 細長い形状のシリカゾルの製造法 |
| US6358882B1 (en) * | 1998-12-08 | 2002-03-19 | The Standard Oil Company | Fluid bed vinyl acetate catalyst |
| US5968473A (en) * | 1998-12-18 | 1999-10-19 | Uop Llc | Stannosilicate molecular sieves |
| DE60003461T2 (de) * | 1999-11-23 | 2004-05-06 | UNIVERSITé LAVAL | Mesoporöses zeolithisches material mit mikroporösen kristallinen mesoporenwänden |
| US6274112B1 (en) * | 1999-12-08 | 2001-08-14 | E. I. Du Pont De Nemours And Company | Continuous production of silica-based microgels |
| US6191323B1 (en) * | 2000-04-25 | 2001-02-20 | Uop Llc | Process for the reduction of ketones and aldehydes to alcohols using a tin substituted zeolite beta |
| US6672993B2 (en) * | 2001-01-12 | 2004-01-06 | Aqualogix, Inc. | Aquatic exercise device |
| US6442795B1 (en) * | 2001-01-16 | 2002-09-03 | Girefa Enterprise Co., Ltd. | Damper for a pivot door |
| JP2003183019A (ja) * | 2001-12-18 | 2003-07-03 | Catalysts & Chem Ind Co Ltd | ゼオライトの濾過分離方法 |
| CN1224590C (zh) * | 2002-05-22 | 2005-10-26 | 吉林大学 | 一种复合磁性粒子的制备方法 |
| US6916514B2 (en) * | 2003-07-18 | 2005-07-12 | Eastman Kodak Company | Cationic shelled particle |
| US20070104643A1 (en) * | 2005-08-05 | 2007-05-10 | Holland Brian T | Mesoporous nanocrystaline zeolite composition and preparation from amorphous colloidal metalosilicates |
| US8052788B2 (en) * | 2005-08-10 | 2011-11-08 | Nalco Company | Method of producing silica sols with controllable broad size distribution and minimum particle size |
| US20070034116A1 (en) * | 2005-08-10 | 2007-02-15 | Mac Donald Dennis L | Silica sols with controlled minimum particle size and preparation thereof |
-
2004
- 2004-04-19 US US10/827,214 patent/US20050234136A1/en not_active Abandoned
-
2005
- 2005-04-13 KR KR1020067021598A patent/KR20070027535A/ko not_active Ceased
- 2005-04-13 CA CA2560748A patent/CA2560748C/en not_active Expired - Lifetime
- 2005-04-13 WO PCT/US2005/012371 patent/WO2005104683A2/en not_active Ceased
- 2005-04-13 CN CN2005800118801A patent/CN1942237B/zh not_active Expired - Lifetime
- 2005-04-13 CN CN2010102460035A patent/CN101912755B/zh not_active Expired - Fee Related
- 2005-04-13 EP EP05735668.5A patent/EP1744825B1/en not_active Expired - Lifetime
- 2005-04-13 SG SG200902613-9A patent/SG152248A1/en unknown
- 2005-04-13 BR BRPI0509859-9A patent/BRPI0509859B1/pt active IP Right Grant
- 2005-04-13 JP JP2007509513A patent/JP5103168B2/ja not_active Expired - Lifetime
- 2005-04-18 TW TW094112213A patent/TWI377980B/zh not_active IP Right Cessation
-
2018
- 2018-01-22 US US15/877,168 patent/US10730756B2/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2913419A (en) | 1956-04-18 | 1959-11-17 | Du Pont | Chemical process and composition |
| US2974108A (en) | 1957-01-14 | 1961-03-07 | Du Pont | Aluminosilicate aquasols and their preparation |
Non-Patent Citations (1)
| Title |
|---|
| See also references of EP1744825A4 |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009018960A (ja) * | 2006-04-04 | 2009-01-29 | Nalco Co | ポリシリケート粒子状材料の製造および使用 |
| JP2010509496A (ja) * | 2006-11-08 | 2010-03-25 | ナルコ カンパニー | 高金属性ケイ質組成物及び同一物を生成する方法 |
| CN101225282B (zh) * | 2007-01-19 | 2013-05-01 | 安集微电子(上海)有限公司 | 一种低介电材料抛光液 |
| CN102344761A (zh) * | 2011-08-03 | 2012-02-08 | 南通海迅天恒纳米科技有限公司 | 一种铈掺杂二氧化硅溶胶的制备方法 |
| WO2013028958A1 (en) | 2011-08-25 | 2013-02-28 | Basf Corporation | Molecular sieve precursors and synthesis of molecular sieves |
| US10087081B2 (en) | 2013-03-08 | 2018-10-02 | Ecolab Usa Inc. | Process for producing high solids colloidal silica |
| EP3368478A4 (en) * | 2015-10-26 | 2019-06-05 | Ecolab USA Inc. | VERY HOMOGENEOUS ZEOLITE PRELUDE |
Also Published As
| Publication number | Publication date |
|---|---|
| EP1744825B1 (en) | 2019-02-27 |
| JP2007532470A (ja) | 2007-11-15 |
| US20180141822A1 (en) | 2018-05-24 |
| CN1942237A (zh) | 2007-04-04 |
| US10730756B2 (en) | 2020-08-04 |
| CN101912755B (zh) | 2012-07-04 |
| BRPI0509859A (pt) | 2007-10-09 |
| JP5103168B2 (ja) | 2012-12-19 |
| CA2560748C (en) | 2013-06-18 |
| CN1942237B (zh) | 2011-07-06 |
| KR20070027535A (ko) | 2007-03-09 |
| US20050234136A1 (en) | 2005-10-20 |
| TW200539935A (en) | 2005-12-16 |
| BRPI0509859B1 (pt) | 2019-04-24 |
| TWI377980B (en) | 2012-12-01 |
| CN101912755A (zh) | 2010-12-15 |
| EP1744825A4 (en) | 2011-09-07 |
| EP1744825A2 (en) | 2007-01-24 |
| CA2560748A1 (en) | 2005-11-10 |
| SG152248A1 (en) | 2009-05-29 |
| WO2005104683A3 (en) | 2006-11-30 |
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