CA2653155A1 - Pelletized silica - Google Patents
Pelletized silica Download PDFInfo
- Publication number
- CA2653155A1 CA2653155A1 CA002653155A CA2653155A CA2653155A1 CA 2653155 A1 CA2653155 A1 CA 2653155A1 CA 002653155 A CA002653155 A CA 002653155A CA 2653155 A CA2653155 A CA 2653155A CA 2653155 A1 CA2653155 A1 CA 2653155A1
- Authority
- CA
- Canada
- Prior art keywords
- particles
- organic solvent
- alcohol
- silica
- water
- Prior art date
- Legal status (The legal status 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 status listed.)
- Granted
Links
Classifications
-
- 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
-
- 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
- C01B33/18—Preparation of finely divided silica neither in sol nor in gel form; After-treatment thereof
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL 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
- C03C1/00—Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels
- C03C1/02—Pretreated ingredients
- C03C1/026—Pelletisation or prereacting of powdered raw materials
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/28—Compounds of silicon
- C09C1/30—Silicic acid
- C09C1/3009—Physical treatment, e.g. grinding; treatment with ultrasonic vibrations
- C09C1/3036—Agglomeration, granulation, pelleting
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/28—Compounds of silicon
- C09C1/30—Silicic acid
- C09C1/3081—Treatment with organo-silicon compounds
-
- 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
- C01P2004/61—Micrometer sized, i.e. from 1-100 micrometer
-
- 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
-
- 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
- C01P2006/16—Pore diameter
-
- 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
- C01P2006/80—Compositional purity
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Materials Engineering (AREA)
- Silicon Compounds (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Glass Compositions (AREA)
- Glass Melting And Manufacturing (AREA)
Abstract
Pelletized silica particles characterized by a round shape and a monomodal particle size distribution are produced by dispersing silica particles into water, adding water to the dispersion, mixing with alkoxisilane, pouring the mixture into an organic solvent, filtering and washing the silica particles obtained. The pelletized silica particles can be used to produce glass monoliths.
Claims (21)
1) Pelletized silica particles, characterized by a round shape and a monomodal particle size distribution.
2) A method for the production of pelletized silica particles according to claim 1, characterized in that, silica particles are dispersed in water at acidic pH
under stirring, an liquid alkoxide silane is then added, the so obtained dispersion is transferred under strong stirring in to a vessel containing an organic solvent, then the pH is raised by the addition of an anorganic base ammonia derivative, the obtained gelly particles are washed with an alcohol and then with a mixture of an alcohol and water, the particles are then filtered and then calcinated at high temperature for at least 1 hour in order to eliminate traces of the solvent from the inorganic oxide particles.
under stirring, an liquid alkoxide silane is then added, the so obtained dispersion is transferred under strong stirring in to a vessel containing an organic solvent, then the pH is raised by the addition of an anorganic base ammonia derivative, the obtained gelly particles are washed with an alcohol and then with a mixture of an alcohol and water, the particles are then filtered and then calcinated at high temperature for at least 1 hour in order to eliminate traces of the solvent from the inorganic oxide particles.
3) The method according to claim 2, characterized in that in which the said silica is fumed silica.
4) The method according to claim 2, characterized in that in which the starting pH of the aqueous solution with silica particles is in the range 1 to 4.
5) The method according to claim 2, characterized in, that said silica is fumed silica.
6) The method according to claim 2, characterized in that the liquid alkoxisilane is tetramethoxysilane and/or tetraethoxysilane.
7) The method according to claim 2, characterized in that said organic solvent is an apolar organic solvent and has a dielectric constant lower than 60 at 20°C.
8) The method according to claim 2 characterized in that the water solution contains a soluble salt to e considered as a doping agent for the final pellets.
9) The method according to claim 7, characterized in that said apolar organic solvent is a liquid alkane such as hexane, eptane, octane, nonane or silicon oil and alcohol such as: propanol, butanol, pentanol, hexanol, eptanol, octanol, nonanol, decanol and a aromatic compound like toluene, benzene, nitrobenzene, chlorobenzene, dichlorobenzene, quinoline, decaline and/or a mixture thereof.
10) The method according to claim 2, characterized in, that said ammonia derivative is cyclohexylamine, t-alkyl amine.
11) The method according to claim 2, characterized in that the pH after the addition of the organic base is in the range from 8 to 12, more preferably from 10 to 12.
12) The method according to claim 2, characterized in that the calcinations temperature is between 300 and 800°C, more preferably between 300 and 600.°
13) A method for the production of pelletized of natura quartz particles according to claim 1, characterized in that, to water at acidic pH under stirring, an liquid alkoxide silane is added, and then under strong stirring natural quartz powder is added to the solution. The so obtained dispersion is transferred under strong stirring in to a vessel containing an organic solvent, then the pH is raised by the addition of an inorganic base ammonia derivative, the obtained gelly particles are washed with an alcohol and then with a mixture of an alcohol and water, the particles are then filtered and then calcinated at high temperature for at least 1 hour in order to eliminate traces of the solvent from the inorganic oxide particles
14) The method according to claim 13, characterized in that in which the starting pH of the aqueous solution with silica particles is in the range 1 to 4.
15) The method according to claim 2, characterized in that the liquid alkoxisilane is tetramethoxysilane and/or tetraethoxysilane.
16) The method according to claim 13, characterized in that said organic solvent is an apolar organic solvent and has a dielectric constant lower than 60 at 20°C.
17) The method according to claim 13 characterized in that the water solution contains a soluble salt to e considered as a doping agent for the final pellets.
18) The method according to claim 7, characterized in that said apolar organic solvent is a liquid alkane such as hexane, eptane, octane, nonane or silicon oil and alcohol such as: propanol, butanol, pentanol, hexanol, eptanol, octanol, nonanol, decanol and a aromatic compound like toluene, benzene, nitrobenzene, chlorobenzene, dichlorobenzene, quinoline, decaline and/or a mixture thereof.
19) The method according to claim 2, characterized in, that said ammonia derivative is cyclohexylamine, t-alkyl amine.
20) The method according to claim 13, characterized in that the pH after the addition of the organic base is in the range from 8 to 12, more preferably from 10 to 12.
21 21) The method according to claim 13, characterized in that the calcinations temperature is between 300 and 800°C, more preferably between 300 and 600.°
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP2006062883 | 2006-06-02 | ||
EPPCT/EP2006/062883 | 2006-06-02 | ||
PCT/EP2007/055365 WO2007141196A1 (en) | 2006-06-02 | 2007-05-31 | Pelletized silica |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2653155A1 true CA2653155A1 (en) | 2007-12-13 |
CA2653155C CA2653155C (en) | 2012-01-24 |
Family
ID=37697918
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA2653155A Expired - Fee Related CA2653155C (en) | 2006-06-02 | 2007-05-31 | Pelletized silica |
Country Status (8)
Country | Link |
---|---|
JP (1) | JP2009538816A (en) |
KR (1) | KR101089897B1 (en) |
CN (1) | CN101460400B (en) |
AU (1) | AU2007255488B2 (en) |
CA (1) | CA2653155C (en) |
NO (1) | NO20084294L (en) |
TW (1) | TWI372139B (en) |
WO (1) | WO2007141196A1 (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2559608A (en) * | 2017-02-13 | 2018-08-15 | Sibelco Nederland N V | Grains comprising silica and methods of forming grains comprising silica |
US10343941B2 (en) * | 2017-06-16 | 2019-07-09 | Owens-Brockway Glass Container Inc. | Glass batch material and process for making glass |
CN111747417A (en) * | 2019-03-28 | 2020-10-09 | 福建通源硅业有限公司 | Preparation method of silicon dioxide particles |
CN110479954A (en) * | 2019-08-19 | 2019-11-22 | 安徽省含山县兴建铸造厂 | A kind of model casting precision casting shell fire resistant covering material |
CN111170344A (en) * | 2020-01-15 | 2020-05-19 | 珠海琴晟新材料有限公司 | Preparation method of ultra-pure nano material |
CN111868159B (en) * | 2020-02-17 | 2022-07-26 | 浙江三时纪新材科技有限公司 | Preparation method of spherical silicon dioxide powder filler, powder filler obtained by preparation method and application of powder filler |
CN111634915A (en) * | 2020-06-12 | 2020-09-08 | 将乐三晶新材料有限公司 | Atomization powder making process for molten metal silicon |
CN115974089B (en) * | 2023-02-17 | 2023-10-20 | 江苏海格新材料有限公司 | Production method of active silicon micropowder |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62260712A (en) * | 1986-05-02 | 1987-11-13 | Toray Ind Inc | Production of silica particle |
EP0725037B2 (en) * | 1995-02-04 | 2012-04-25 | Evonik Degussa GmbH | Granules on the basis of pyrogenic silica, process for their preparation and use thereof |
JPH08281095A (en) * | 1995-02-14 | 1996-10-29 | Toyota Motor Corp | Dilatant liquid |
DE10123950A1 (en) * | 2001-05-17 | 2002-11-28 | Degussa | Granules based on pyrogenic silicon dioxide doped with aluminum oxide by means of aerosol, process for their production and their use |
DE10256267A1 (en) * | 2002-12-03 | 2004-06-24 | Degussa Ag | Dispersion, coating color and recording medium |
DE102004011110A1 (en) * | 2004-03-08 | 2005-09-22 | Merck Patent Gmbh | Process for producing monodisperse SiO 2 particles |
-
2007
- 2007-05-30 TW TW096119361A patent/TWI372139B/en not_active IP Right Cessation
- 2007-05-31 AU AU2007255488A patent/AU2007255488B2/en not_active Ceased
- 2007-05-31 JP JP2009512608A patent/JP2009538816A/en active Pending
- 2007-05-31 CN CN2007800205334A patent/CN101460400B/en not_active Expired - Fee Related
- 2007-05-31 CA CA2653155A patent/CA2653155C/en not_active Expired - Fee Related
- 2007-05-31 WO PCT/EP2007/055365 patent/WO2007141196A1/en active Application Filing
- 2007-05-31 KR KR1020087029435A patent/KR101089897B1/en not_active IP Right Cessation
-
2008
- 2008-10-14 NO NO20084294A patent/NO20084294L/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
CA2653155C (en) | 2012-01-24 |
NO20084294L (en) | 2009-01-09 |
TWI372139B (en) | 2012-09-11 |
TW200815284A (en) | 2008-04-01 |
AU2007255488B2 (en) | 2011-01-27 |
AU2007255488A1 (en) | 2007-12-13 |
JP2009538816A (en) | 2009-11-12 |
CN101460400B (en) | 2011-09-14 |
KR101089897B1 (en) | 2011-12-05 |
CN101460400A (en) | 2009-06-17 |
KR20090009290A (en) | 2009-01-22 |
WO2007141196A1 (en) | 2007-12-13 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKLA | Lapsed |
Effective date: 20140602 |