CN102826736A - Method for preparing hollow glass bead by using glass powder process - Google Patents
Method for preparing hollow glass bead by using glass powder process Download PDFInfo
- Publication number
- CN102826736A CN102826736A CN2012103523971A CN201210352397A CN102826736A CN 102826736 A CN102826736 A CN 102826736A CN 2012103523971 A CN2012103523971 A CN 2012103523971A CN 201210352397 A CN201210352397 A CN 201210352397A CN 102826736 A CN102826736 A CN 102826736A
- Authority
- CN
- China
- Prior art keywords
- glass
- hollow
- crushing
- molten glass
- powder
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/10—Forming beads
- C03B19/107—Forming hollow beads
- C03B19/1075—Forming hollow beads by blowing, pressing, centrifuging, rolling or dripping
Abstract
The invention discloses a method for preparing a hollow glass bead by using a glass powder process, comprising the following steps of: proportioning, melting, crushing, hollow balling, collecting, screening and inspecting. The crushing step is operated as follows: molten glass is sprayed out through a porous nozzle under the action of high-pressure gas of over 2MPa to form downwards splashed molten glass drops, the molten glass drops runs into the surface of a high-speed rotating rotary drum in the falling process, circulating water is introduced to the rotary drum to cool the molten glass drops, and molten glass drops form glass particles with particle sizes of 1-100mm under the combined actions of gravity, centrifugal force and splashing force. The method has the innovation point that a novel centrifugal crushing process is used for replacing the water crushing, drying, coarse crushing and fine crushing processes in the original production process, and therefore, the production process is simplified, the energy consumption is reduced, equipment and personnel costs are reduced, and operation and quality are easy to control; and by using the method, the production cost can be reduced by 14-20%, and the compression strength is improved by 4.8-15%.
Description
Technical field:
The present invention relates to the production technique of hollow glass micropearl, in particular, relate to the method that a kind of glass powder legal system is equipped with hollow glass micropearl.
Background technology:
Hollow glass micropearl is a kind of hollow, include the spherical glass powder of one or more rare gas elementes, size distribution from several microns to hundreds of micron.Particular structure makes it to possess that density is low, good fluidity, thermal conductivity is low, ultimate compression strength is high, chemicalstability is good characteristics, has been applied in military, civilian and high-tech areas such as aerospace, oil production, deep-sea floating body material, emulsion [explosive, high-grade insulating materials, body of wall heat-insulating fire-proofing material at present.
The preparation method of hollow glass micropearl mainly contains desiccant gel method, sessile drop method and glass powder method; Because preparing method's restriction; The hollow glass micropearl intensity of desiccant gel method and sessile drop method preparation is all lower, and the glass powder method is generally adopted in the production of high-end hollow glass micropearl.
Glass powder method production process mainly is: 1 batching → 2 fusings → 3 water are broken → 4 oven dry → 5 coarse crushings → 6 are in small, broken bits → 7 hollow nodularizations → 8 collect → 9 screenings → 10 checks, and the batching fusing is to prepare dissimilar products as requested, hollow nodularization be formed product must be through process; Be comparatively ripe at present and stable technology; To consider from industrialized angle, 3 water are broken → and the operating process in small, broken bits of 4 oven dry → 5 coarse crushings → 6 is loaded down with trivial details relatively, complex manufacturing; Equipment is many; Energy consumption is high, and efficient is low, increases the uncontrollability of product.This segment process detailed process is: at first will melt good glass metal and pour slowly from melting furnaces that through the shrend chilling glass metal to be become glass in the tank that feeds cold water broken into; Pull it out oven dry and the glass that it is broken for below 2 millimeters is broken then through roll crusher; Standard compliant glass is broken to be sent in the airflow milling, and pulverizing is 1~100 micron a glass powder.In the shattering process since the introducing of impurity such as iron cause the glass microballon composition change, reduced the hollow glass micropearl performance index, bring noise and dust pollution simultaneously; Because the input of the energy and human cost has strengthened production cost, because the increase of control node has increased difficulty also for the quality control of hollow glass micropearl.
Summary of the invention
The object of the present invention is to provide a kind of glass powder legal system that is easy to operate and control to be equipped with the method for hollow glass micropearl, production cost reduces by 14~20%, and ultimate compression strength improves 4.8~15%.
The objective of the invention is through pulverising step among the preparation technology being improved as follows realization; A kind of glass powder legal system is equipped with the method for hollow glass micropearl; Comprise batching, fusion, pulverizing, hollow nodularization, collection, screening, check; Innovative point of the present invention be with water in the existing production technique broken → oven dry → coarse crushing → process in small, broken bits is reduced to centrifugal pulverizing one step completion; Said pulverising step is operated as follows: the glass metal after the fusing sprays through porous nozzle under the above high pressure gas effect of 2MPa; Make it to form the melten glass drop that splashes down downwards; The melten glass drop in dropping process with the collision of the drum surface of high speed rotating, feed the recirculated water cooling in the rotary drum, the acting in conjunction that glass metal drops in gravity, cf-, sputter power form down particle diameter between 1~100 micron glass particle and get rid of in the powder collecting bin.
The further technical scheme of the present invention is that said glass drop forms the size of particle diameter through regulating the pressure-controlling of rotary drum rotating speed and sparging gases.
The present invention is directed to glass powder method hollow glass micropearl production technique improves; Adopt a kind of new centrifugal pulverizing replace in the original production process water broken → oven dry → coarse crushing → process in small, broken bits; Simplified production technique, cut down the consumption of energy, minimizing equipment and personnel cost; Operation is easy to control with quality, and the shrend effect is also better; The present invention can reduce production costs 14~20%, improves ultimate compression strength 4.8~15%.
Embodiment
Embodiment 1
Adopting product density is 0.25 g/cm
3Glass formula configuration frit; The frit for preparing and mix is put into kiln carry out fusion; 1500 ℃~1600 ℃ of glass melting temperatures; Melting time is 1~3 hour, and melten glass liquid sprays downwards through porous nozzle under the high pressure gas effect of 2.4Mpa, forms the high speed glass drop that sputters fast downwards; And in dropping process with the collision of the high speed drum surface of 900r/min, glass metal drops under the acting in conjunction of gravity, cf-, sputter power and gets rid of into the glass powder of meta particle diameter about 15 microns.Glass powder and air mixed are sprayed into into the pearl stove, rapid hollow nodularization in 1580 ℃ temperature field.Powder after the hollow nodularization is mainly collected through tornado dust collector, and remaining superfine powder is collected through bagroom.The powder of collecting utilizes hollow glass micropearl to winnow the device sorting, and hollow glass micropearl and glass microballon are separated, and dries classification simultaneously, and producing density is 0.25 ± 0.02g/cm
3, ultimate compression strength 9Mp, the hollow glass micropearl of its floatability>=98%, ultimate compression strength improves 12.5%, and production cost reduces by 19%.
Embodiment 2
The employing product density is 0.4g/cm
3Glass formula configuration frit; The frit for preparing and mix is put into kiln carry out fusion; 1480~1580 ℃ of glass melting temperatures; Melting time is 1~3 hour, and melten glass liquid sprays downwards through porous nozzle under the high pressure gas effect of 2.2Mpa, forms the high speed glass drop that sputters fast downwards; And in dropping process with the collision of the high speed drum surface of 800r/min, glass metal drops under the acting in conjunction of gravity, cf-, sputter power and gets rid of into the glass powder of meta particle diameter about 20 microns.Glass powder and air mixed are sprayed into into the pearl stove, rapid hollow nodularization in 1540 ℃ temperature field.Powder after the hollow nodularization is mainly collected through tornado dust collector, and remaining superfine powder is collected through bagroom.The powder of collecting utilizes hollow glass micropearl to winnow the device sorting, and hollow glass micropearl and glass microballon are separated, and dries classification simultaneously, and producing density is 0.4 ± 0.02g/cm
3, ultimate compression strength 40 Mp, the hollow glass micropearl of its floatability>=95%, ultimate compression strength improves 11.1%, and production cost can reduce by 17%.
Embodiment 3
The employing product density is 0.7g/cm
3Glass formula configuration frit; The frit for preparing and mix is put into kiln carry out fusion; 1450~1550 ℃ of glass melting temperatures; Melting time is 1~3 hour, and melten glass liquid sprays downwards through porous nozzle under the high pressure gas effect of 2.1Mpa, forms the high speed glass drop that sputters fast downwards; And in dropping process with the collision of the high speed drum surface of 700r/min, glass metal drops under the acting in conjunction of gravity, cf-, sputter power and gets rid of into the glass powder of meta particle diameter about 25 microns.Glass powder and air mixed are sprayed into into the pearl stove, rapid hollow nodularization in 1500 ℃ temperature field.Powder after the hollow nodularization is mainly collected through tornado dust collector, and remaining superfine powder is collected through bagroom.The powder of collecting utilizes hollow glass micropearl to winnow the device sorting, and hollow glass micropearl and glass microballon are separated, and dries classification simultaneously, and producing density is 0.7 ± 0.02g/cm
3, ultimate compression strength 131 Mp, the hollow glass micropearl of its floatability>=96%, ultimate compression strength improves 5%, and production cost reduces by 14%.
Should be noted that so-called ultimate compression strength refers to applies the isostatic pressure via gas or liquid conductive to hollow glass micropearl, and intensity corresponding when hollow glass micropearl breaks 10% (volume ratio) is its ultimate compression strength.Concrete data contrast can see Table one.The ultimate compression strength of three different ingredients hollow glass micropearls, density and cost analysis.
Table one
The above only is preferred embodiment of the present invention, is not the present invention is done any pro forma restriction; Any those of ordinary skill in the art; Do not breaking away under the technical scheme scope situation of the present invention; All the method for above-mentioned announcement capable of using and technology contents are made many possible changes and modification to technical scheme of the present invention, or are revised as the equivalent embodiment of equivalent variations.Therefore, every content that does not break away from technical scheme of the present invention, according to technical spirit of the present invention to any simple modification that above embodiment did, be equal to replacement, equivalence changes and modify, all still belong in the scope that technical scheme of the present invention protects.
Claims (2)
1. a glass powder legal system is equipped with the method for hollow glass micropearl; Comprise batching, fusion, pulverizing, hollow nodularization, collection, screening, check; It is characterized in that; Said pulverising step is operated as follows: the glass metal after the fusing through the porous nozzle ejection, makes it to form the melten glass drop that splashes down downwards under the above high pressure gas effect of 2MPa, and the melten glass drop collides with the drum surface of high speed rotating in dropping process; Feed the recirculated water cooling in the rotary drum, the acting in conjunction that glass metal drops in gravity, cf-, sputter power form down particle diameter between 1~100 micron glass particle and get rid of in the powder collecting bin.
2. a kind of glass powder legal system according to claim 1 is equipped with the method for hollow glass micropearl, it is characterized in that, said glass drop forms the size of particle diameter through regulating the pressure-controlling of rotary drum rotating speed and sparging gases.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012103523971A CN102826736A (en) | 2012-09-21 | 2012-09-21 | Method for preparing hollow glass bead by using glass powder process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012103523971A CN102826736A (en) | 2012-09-21 | 2012-09-21 | Method for preparing hollow glass bead by using glass powder process |
Publications (1)
Publication Number | Publication Date |
---|---|
CN102826736A true CN102826736A (en) | 2012-12-19 |
Family
ID=47330082
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2012103523971A Pending CN102826736A (en) | 2012-09-21 | 2012-09-21 | Method for preparing hollow glass bead by using glass powder process |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102826736A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103755146A (en) * | 2013-12-14 | 2014-04-30 | 蚌埠玻璃工业设计研究院 | Solid floating material hollow glass microbead, and preparation method thereof |
CN103979862A (en) * | 2014-04-15 | 2014-08-13 | 吴春池 | Energy-saving and environmental-protection material, preparation method and application of energy-saving and environmental-protection material in building system |
CN104891788A (en) * | 2015-05-30 | 2015-09-09 | 连云港浩特石英材料有限公司 | Preparation method of fused quartz hollow spheres |
CN108609843A (en) * | 2018-04-20 | 2018-10-02 | 郭宝华 | A kind of device and method producing flakey material with raw mineral materials |
CN109689582A (en) * | 2016-06-27 | 2019-04-26 | Bpi珠子生产国际有限公司 | Method and apparatus for producing hollow glass microbead |
CN110818271A (en) * | 2019-12-03 | 2020-02-21 | 陈保军 | Preparation method of high-refractive-index glass beads |
CN111170645A (en) * | 2020-01-15 | 2020-05-19 | 浙江工业大学 | Glass micropowder containing nano particles and preparation method thereof |
CN115818931A (en) * | 2022-12-02 | 2023-03-21 | 中建材玻璃新材料研究院集团有限公司 | Preparation method of ultra-light low-heat-conduction hollow glass microspheres |
CN116023009A (en) * | 2023-02-17 | 2023-04-28 | 淄博康建科技陶瓷有限公司 | Light glass microbead and preparation process thereof |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3495961A (en) * | 1966-12-27 | 1970-02-17 | Potter Brothers Inc | Method and apparatus for vitreous bead manufacture |
US3877914A (en) * | 1973-06-18 | 1975-04-15 | Potters Industries Inc | Method and apparatus for making glass spheres |
GB1553542A (en) * | 1977-08-25 | 1979-09-26 | Sumitomo Metal Ind | Method and apparatus for granulating metallurgical slag |
US4215084A (en) * | 1978-05-03 | 1980-07-29 | The Battelle Development Corporation | Method and apparatus for producing flake particles |
CN1316308A (en) * | 2001-02-26 | 2001-10-10 | 沈阳工业大学 | Planar slip casting technology for making powder and its technological equipment |
CN101638295A (en) * | 2008-07-30 | 2010-02-03 | 中国建材国际工程有限公司 | Hollow glass microballoons and production method thereof |
-
2012
- 2012-09-21 CN CN2012103523971A patent/CN102826736A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3495961A (en) * | 1966-12-27 | 1970-02-17 | Potter Brothers Inc | Method and apparatus for vitreous bead manufacture |
US3877914A (en) * | 1973-06-18 | 1975-04-15 | Potters Industries Inc | Method and apparatus for making glass spheres |
GB1553542A (en) * | 1977-08-25 | 1979-09-26 | Sumitomo Metal Ind | Method and apparatus for granulating metallurgical slag |
US4215084A (en) * | 1978-05-03 | 1980-07-29 | The Battelle Development Corporation | Method and apparatus for producing flake particles |
CN1316308A (en) * | 2001-02-26 | 2001-10-10 | 沈阳工业大学 | Planar slip casting technology for making powder and its technological equipment |
CN101638295A (en) * | 2008-07-30 | 2010-02-03 | 中国建材国际工程有限公司 | Hollow glass microballoons and production method thereof |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103755146A (en) * | 2013-12-14 | 2014-04-30 | 蚌埠玻璃工业设计研究院 | Solid floating material hollow glass microbead, and preparation method thereof |
CN103979862A (en) * | 2014-04-15 | 2014-08-13 | 吴春池 | Energy-saving and environmental-protection material, preparation method and application of energy-saving and environmental-protection material in building system |
CN103979862B (en) * | 2014-04-15 | 2015-10-07 | 吴春池 | A kind of energy-conserving and environment-protective material, preparation method and the application in building system thereof |
CN104891788A (en) * | 2015-05-30 | 2015-09-09 | 连云港浩特石英材料有限公司 | Preparation method of fused quartz hollow spheres |
CN109689582A (en) * | 2016-06-27 | 2019-04-26 | Bpi珠子生产国际有限公司 | Method and apparatus for producing hollow glass microbead |
CN108609843B (en) * | 2018-04-20 | 2021-07-27 | 郭宝华 | Device and method for producing flaky material by using mineral raw material |
CN108609843A (en) * | 2018-04-20 | 2018-10-02 | 郭宝华 | A kind of device and method producing flakey material with raw mineral materials |
CN110818271A (en) * | 2019-12-03 | 2020-02-21 | 陈保军 | Preparation method of high-refractive-index glass beads |
CN110818271B (en) * | 2019-12-03 | 2023-05-19 | 绵阳光耀新材料有限责任公司 | Preparation method of high-refractive-index glass beads |
CN111170645A (en) * | 2020-01-15 | 2020-05-19 | 浙江工业大学 | Glass micropowder containing nano particles and preparation method thereof |
CN115818931A (en) * | 2022-12-02 | 2023-03-21 | 中建材玻璃新材料研究院集团有限公司 | Preparation method of ultra-light low-heat-conduction hollow glass microspheres |
CN116023009A (en) * | 2023-02-17 | 2023-04-28 | 淄博康建科技陶瓷有限公司 | Light glass microbead and preparation process thereof |
CN116023009B (en) * | 2023-02-17 | 2023-06-23 | 淄博康建科技陶瓷有限公司 | Light glass microbead and preparation process thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102826736A (en) | Method for preparing hollow glass bead by using glass powder process | |
CN107309434B (en) | Preparation method and application of high-purity compact spherical molybdenum powder | |
EP2014621A1 (en) | Process for producing glass | |
CN103723910B (en) | A kind of preparation method of porous glass beads | |
CN107838431A (en) | A kind of spherical rhenium powder, preparation method thereof | |
US20070186587A1 (en) | Method for the manufacture of foam glass pellets | |
JP5605902B2 (en) | Method for producing silica glass crucible, silica glass crucible | |
JP5644955B2 (en) | Granulation method of sintering raw material | |
CN103588391B (en) | A kind of hollow glass micropearl and preparation method thereof | |
TWI650290B (en) | Method for producing glass raw material granules, method for producing molten glass, and method for producing glass articles | |
JPWO2013012040A1 (en) | Method for producing molten glass and method for producing glass product | |
CN105417949A (en) | Method for preparing alumina silicate fibers | |
Mucsi et al. | Physical characteristics and technology of glass foam from waste cathode ray tube glass | |
CN104355546A (en) | Foam glass using basalt glass clinker and CRT (cathode ray tube) screen glass as main raw materials and preparation method of foam glass | |
CN106957151A (en) | Soda lime borosilicate hollow glass micropearl and its production method containing rare earth | |
CN104478422B (en) | A kind of without sodium novel high-strength vitrified bond and preparation method thereof | |
JP2022504875A (en) | Method for manufacturing ceramic particle mixture | |
CN104673098B (en) | Preparation technique of cerium-oxide-base rare-earth polishing powder | |
EP4299519A1 (en) | Silica powder and production method therefor | |
KR101365249B1 (en) | Method of manufacturing granulated silica powder and method of manufacturing vitreous silica crucible | |
CN103044030A (en) | Manufacturing method of ceramic beads suitable for sand blasting | |
CN110386608B (en) | Preparation method of light spherical silicon dioxide | |
JP2006193373A (en) | Fine glass bubble and method of manufacturing the same | |
CN104193351A (en) | System and method for producing fracturing propping agent by taking red mud as raw material | |
CN106396696B (en) | The preparation method of mullite spherical shape aggregate enhancing refractory material |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20121219 |