WO2021135881A1 - Method for preparing micro optical glass device - Google Patents

Method for preparing micro optical glass device Download PDF

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Publication number
WO2021135881A1
WO2021135881A1 PCT/CN2020/135095 CN2020135095W WO2021135881A1 WO 2021135881 A1 WO2021135881 A1 WO 2021135881A1 CN 2020135095 W CN2020135095 W CN 2020135095W WO 2021135881 A1 WO2021135881 A1 WO 2021135881A1
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Prior art keywords
optical glass
micro
glass device
value
silica dispersion
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PCT/CN2020/135095
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French (fr)
Chinese (zh)
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陈雨叁
李乾
刘莹莹
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深圳市绎立锐光科技开发有限公司
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Publication of WO2021135881A1 publication Critical patent/WO2021135881A1/en

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    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B19/00Other methods of shaping glass
    • C03B19/12Other methods of shaping glass by liquid-phase reaction processes
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/113Silicon oxides; Hydrates thereof
    • C01B33/12Silica; Hydrates thereof, e.g. lepidoic silicic acid
    • C01B33/16Preparation of silica xerogels
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B19/00Other methods of shaping glass
    • C03B19/10Forming beads
    • C03B19/1005Forming solid beads
    • C03B19/106Forming solid beads by chemical vapour deposition; by liquid phase reaction
    • C03B19/1065Forming solid beads by chemical vapour deposition; by liquid phase reaction by liquid phase reactions, e.g. by means of a gel phase
    • GPHYSICS
    • G02OPTICS
    • G02BOPTICAL ELEMENTS, SYSTEMS OR APPARATUS
    • G02B1/00Optical elements characterised by the material of which they are made; Optical coatings for optical elements
    • 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/50Glass production, e.g. reusing waste heat during processing or shaping
    • Y02P40/57Improving the yield, e-g- reduction of reject rates

Definitions

  • the invention relates to the technical field of glass preparation, in particular to a method for preparing a micro-optical glass device.
  • micro-optical devices such as microlens arrays
  • the method of processing microstructures such as grinding
  • the sol-gel method is relatively More economical preparation method.
  • the traditional sol-gel process with high solid content and low shrinkage rate is suitable for the preparation of large-sized glass devices. Due to the influence of the mold processing size, it is impossible to directly produce micron-level fine optical structures.
  • the inventor applied the traditional low-shrinkage solution sol-gel process to the large-shrinkage solution design, and found that unexpected problems such as excessive gel speed and microstructure deformation would occur, making it difficult to obtain satisfactory products.
  • the present invention provides a method for preparing a micro-optical glass device, which includes the following steps: Step 1: Obtain a silica dispersion, and add an acid solution to the The silica dispersion liquid to adjust the pH value of the silica dispersion liquid to the first pH value and stir; Step 2: adding ethyl orthosilicate to the silica dispersion liquid and stirring to obtain Sol, adding an alkaline solution to the sol to adjust the pH value of the sol to the second pH value, stirring and standing; Step 3: Injecting the standing sol into a mold, aging, and obtaining wet coagulation Glue; Step 4: demold the wet gel, wash and dry to obtain a dry gel; Step 5: sinter the dry gel to obtain a micro-optical glass device; wherein, the range of the second pH value Is 3.0 to 4.0, the shrinkage rate of the micro-optical glass device relative to the wet gel is
  • the molar ratio of silica contained in the silica dispersion to the ethyl orthosilicate is 3.8 to 4.6.
  • the solid content of silicon dioxide in the raw material is not more than 21%, and the solid content means that the silicon dioxide and the ethyl orthosilicate contained in the silicon dioxide dispersion can be hydrolyzed to produce The total amount of silica accounts for the mass percentage of all raw materials.
  • the step one includes: obtaining a silica dispersion stock solution with a preset molar volume, and mixing the silica dispersion stock solution with deionized water to obtain the silica dispersion
  • the deionized water is used to adjust the solid content of the silica.
  • the second pH value ranges from 3.4 to 4.0.
  • the acidic solution is a hydrochloric acid solution
  • the first pH value ranges from 1.3 to 2.8.
  • the mold is a silicone mold.
  • the sintering temperature is not higher than 1200°C.
  • the drying includes a first drying stage and a second drying stage, and the temperature of the first drying stage is at least 100° C. lower than the temperature of the second drying stage.
  • the smallest microstructure size of the micro-optical glass device is not greater than 1 ⁇ m.
  • the present invention includes the following beneficial effects: a sol-gel with a large shrinkage ratio is used to prepare optical glass devices, a pH value lower than the general process is used in the gel stage, and suitable silica and orthosilicic acid are selected.
  • the ratio of ethyl ester not only ensures easy gelation, but also avoids excessively fast gelation, and optical glass devices with fine structures can be obtained at one time.
  • Figure 1 is a schematic flow chart of the method for preparing the micro-optical glass device of the present invention.
  • the main inventive concept is to control the ratio of the two silica sources for preparing glass devices by the sol-gel method and the gel conditions under the ratio, so as to obtain a large shrinkage ratio.
  • the silica dispersion liquid obtained by dispersing fumed silica powder in water has the function of slowing down the gel speed and avoiding the cracking caused by the too fast hydrolysis of the ethyl orthosilicate, and the pH value control during the gel process is very important for the control.
  • the gel speed has a huge impact, and the present invention combines the two to solve the problem of microstructure yield newly encountered in the process of preparing glass devices with large shrinkage rates.
  • the solid content in the present invention refers to the mass percentage of silicon dioxide in the raw materials (including silicon dioxide after the hydrolysis of ethyl orthosilicate) in the total raw materials.
  • Figure 1 is a schematic flow chart of the method for preparing the micro-optical glass device of the present invention, including: step one, obtaining a silica dispersion liquid, and adjusting to a first pH; step two, combining the silica dispersion liquid with Ethyl orthosilicate is mixed and adjusted to the second pH value; step three, preparing wet gel; step four, preparing dry gel; step five, sintering, to obtain micro-optical glass device. Each step is described in detail below.
  • This step includes obtaining a silica dispersion liquid, adding an acidic solution to the silica dispersion liquid to adjust the pH value of the silica dispersion liquid to a first pH value, and stirring, to finally obtain silica with a preset pH value
  • the dispersion is used as the first silica source.
  • the initial silica dispersion (that is, the pH value is not adjusted) can be obtained by mixing and stirring fumed silica and deionized water, and dispersing by magnetic stirring, homogenizer and/or ultrasonic, so that the gas phase Silica is evenly dispersed in water. Then, the silica dispersion is filtered to remove impurities and undispersed agglomerated particles.
  • the fumed silica in the present invention selects a particle size with a D50 in the range of 20 nm to 150 nm, and has a larger specific surface area.
  • a large amount of silica dispersion stock solution with a preset molar volume is prepared in advance, and a certain amount of silica dispersion stock solution is obtained during each production, and mixed and diluted with deionized water.
  • deionized water is used to adjust the solid content of silica, so as to obtain the silica dispersion of the production batch.
  • the acidic solution is added to the silica dispersion and stirred uniformly.
  • the acidic solution can be, for example, a dilute hydrochloric acid solution, so that the silica dispersion is adjusted to a pH value of 1.3-2.8. It can be understood that the acidic solution may also be other acidic solutions for adjusting the pH value.
  • ethyl orthosilicate is added to the silica dispersion and stirred, and the ethyl orthosilicate is hydrolyzed to obtain a sol, and an alkaline solution is further added to the sol to adjust the sol PH value to the second pH value, stir and let stand.
  • the sol will gradually form a gel. The process should not be too long, and it only needs to stand for a short time to expel the bubbles during the stirring process.
  • the alkaline solution may be an aqueous ammonia solution. After the pH value of the sol is adjusted, the pH value increases, and finally is 3.0-4.0. It can be understood that the alkaline solution may also be other alkaline solutions for adjusting the pH value.
  • step 3 since there is a process of standing in the original container (not mold) from step 2 to step 3, and this process is very important to avoid bubbles in the final product, so the gelation process of the sol It should not be too fast, otherwise it will be difficult to transfer it to the mold before the gel is set.
  • the inventor has concluded that since the second pH value exceeds 4.0, step 3 is obviously affected, and the surface microstructure of the obtained wet gel is not clear.
  • a method of reducing the solid content of silica is adopted so that the solid content of silica in the raw material is not more than 21%.
  • a high solid content ratio of raw materials is generally used, usually at least 25% or more. This type of preparation method is difficult to achieve the formation of tiny optical structures.
  • the static sol is poured into a mold and aged to obtain a wet gel.
  • the mold can be of various shapes and sizes as required, so that glass optical devices of various shapes and sizes can be obtained.
  • the wet gel has a certain strength and can be demolded from the mold.
  • the present invention preferably adopts a silicone mold to peel off the wet gel within a certain deformation range of the silicone mold. If a rigid mold is used, on the one hand, it may damage the fine optical surface structure, causing burrs and cracks, and on the other hand, it is not easy to remove the wet gel.
  • the wet gel is demolded, washed and dried to obtain a dry gel.
  • the temperature should not be too high, otherwise it may cause excessive dehydration and cause the sample to crack.
  • the drying step includes two steps, that is, it includes a first drying stage and a second drying stage.
  • the temperature in the first drying stage is at least 100° C. lower than the temperature in the second drying stage to avoid violent separation of water from the wet gel during the drying process and causing cracking.
  • the first drying stage is carried out in an air atmosphere, and the drying temperature is 30°C to 90°C; the second drying stage is carried out in an oxygen-free and moisture-free atmosphere, and the drying temperature is 150°C to 500°C. °C.
  • the dry gel is sintered to obtain a micro-optical glass device.
  • the sample gets a second volume shrinkage, and changes from opaque to transparent glass device.
  • sintering needs to be performed at a temperature above 1200°C.
  • the inventor found that sintering at high temperatures will damage the edges and surfaces of optical glass devices, causing them to slightly deform or even deform. Cracked.
  • traditional larger-sized optical glass devices such as millimeter-level optical devices
  • such surface defects have little effect, but in micro-optical glass devices, this will seriously affect the optical performance of the device.
  • the inventor found that by reducing the solid content of silica in the raw material, an optical device with high transparency can be obtained even if the sintering temperature is lowered.
  • the sintering temperature is not higher than 1200°C, which not only protects the micro-optical structure of the glass surface from cracking, but also reduces the risk of internal crystallization and decreased transparency at low solid content, and improves the product yield. .
  • the reduction of sintering temperature can also reduce energy consumption and production costs.
  • Second, weigh the fumed silica particles and deionized water, mix and stir, use a homogenizer to disperse evenly; add dilute hydrochloric acid, adjust pH 2, after stirring, add ethyl orthosilicate, stir to form a sol solution, and then add ammonia Adjust the sol to the second pH value, stir and then stand still, pour it into a mold with a microstructure, wait for a certain period of time to gel, and then leave it to stand for a preset time before demolding.
  • wet gel with microstructure in pure deionized water, wash it with circulating water, after washing, put it into a constant temperature and humidity box at 45°C for the first stage of drying, and then carry out the second stage in a nitrogen atmosphere at 200°C Staged drying. After the sample is dried, it is sintered at 1100°C for 12 hours to obtain an optical element with a microstructure.
  • the ratio is the substance of silica (SiO 2) contained in the fumed silica particles or silica dispersion stock solution
  • the shrinkage rate is the volume shrinkage rate of the sintered glass device relative to the gel after demolding, which can be passed through Archimedes Method measurement
  • Yield rate refers to defective products with cracks, scratches, dirt, bubbles, and extremely low transmittance.
  • the research on the second pH value and n SiO2 /n TEOS is based on the background of large shrinkage rate.
  • the shrinkage rate of the micro-optical glass device prepared by the present invention is greater than 88% relative to the wet gel. The shrinkage will cause problems such as the complete shape of the micro-optical structure molding.
  • the surface can absorb a certain amount of OH-, and through molecular vibration and chemical bond breakage, SiO- will be produced, which can attack the central Si atom of other sol molecules and cause condensation reaction.
  • the condensation reaction mechanism is a nucleophilic reaction mechanism.
  • the inventor found through repeated experiments that when the second pH value is lower than 3.0, the gel time is long, and even if the gel is obtained, the prepared sample is extremely easy to crack; as the pH value increases, the gel time is shortened, The yield rate of the glass device obtained by drying and sintering the sample after the gel is gradually improved; however, when the pH value exceeds 4.0, the gel speed is too fast, which is not conducive to the formation of microstructure.
  • the minimum microstructure size of the micro-optical device is not greater than 1 ⁇ m, and it is difficult to form the microstructure if the second pH value exceeds 4.0.
  • Ethyl orthosilicate contributes to the gel process. If only silica dispersion is used as the silica source, the gel formation process is extremely slow and cannot be used in mass production of products. The amount of ethyl orthosilicate, the required gel time is gradually shortened. According to the inventor's research, the molar ratio n SiO 2 /n TEOS of silicon dioxide to tetraethyl orthosilicate contained in the silicon dioxide dispersion liquid is below 5.4, which can meet the mass production requirements.
  • the solution that does not require a 100% yield rate is adopted.
  • the yield rate and production time need to be considered comprehensively.
  • a higher yield rate often represents a longer gel time, as long as the number of good products per unit time is higher. That's it.
  • the molar ratio of silica to tetraethyl orthosilicate contained in the silica dispersion is 3.8 to 5.4.
  • the molar ratio of silica to tetraethyl orthosilicate contained in the silica dispersion is 3.8 to 4.6.

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Abstract

Disclosed is a method for preparing a micro optical glass device with a low cost and a simple process. The method comprises: obtaining a silica dispersion, adding an acidic solution into the silica dispersion to adjust the pH value of the silica dispersion to a first pH value, and stirring same; adding ethyl orthosilicate into the silica dispersion, and stirring same to obtain a sol, adding a basic solution into the sol to adjust the pH value of the sol to a second pH value, stirring same and leaving same to stand; injecting the sol, which has been left to stand, into a mold, and aging same to obtain a wet gel; demolding the wet gel, washing same, and drying same to obtain a dry gel; and sintering the dry gel to obtain the micro optical glass device, wherein the second pH value is in the range of 3.0-4.0, the shrinkage of the micro optical glass device is more than 88% relative to that of the wet gel, and the molar ratio of the silica to the ethyl orthosilicate contained in the silica dispersion is in the range of 3.8-5.4. The method ensures a good yield at a large shrinkage during the preparation of a sol-gel.

Description

一种微光学玻璃器件的制备方法Method for preparing micro-optical glass device 技术领域Technical field
本发明涉及玻璃制备技术领域,特别涉及一种微光学玻璃器件的制备方法。The invention relates to the technical field of glass preparation, in particular to a method for preparing a micro-optical glass device.
背景技术Background technique
近年来,随着投影领域的光学设计技术的飞速发展,大而笨重的投影机逐渐为结构精巧、体积小的便携投影机所取代,而且投影技术有着进一步向智能终端如手机、智能眼镜迁移的趋势。伴随而来的是,光机体积的减小及光斑尺寸的减小对光束精细化整形和调制提出了越来越高的要求。而且,随着高亮度激光光源的普及,在满足上述精细化光整形调制的条件下,光学元件也要承受越来越高的热能,从而对耐热性也有了更高的要求,树脂类光学器件已不能满足当前的光机设计,玻璃光学器件已经成为必选项。In recent years, with the rapid development of optical design technology in the projection field, large and cumbersome projectors have gradually been replaced by portable projectors with compact and small size, and projection technology has further migrated to smart terminals such as mobile phones and smart glasses. trend. Concomitantly, the reduction of the volume of the optical machine and the reduction of the spot size have put forward higher and higher requirements for the fine shaping and modulation of the beam. Moreover, with the popularization of high-brightness laser light sources, optical components have to withstand higher and higher heat energy under the conditions of the above-mentioned refined light shaping and modulation, and thus have higher requirements for heat resistance. Resin optics Devices can no longer meet the current opto-mechanical design, and glass optical devices have become a must.
当制备微光学器件(如微透镜阵列)时,在整块玻璃上进行微结构加工(如打磨)的方法,设备成本高且工艺难度大,不利于大规模生产,而溶胶凝胶法是相对较为经济的制备方法。传统的高固含量、低收缩率方案的溶胶凝胶工艺适合制备大尺寸的玻璃器件,受模具加工尺寸的影响,无法直接制得微米级的精细光学结构。When preparing micro-optical devices (such as microlens arrays), the method of processing microstructures (such as grinding) on a whole piece of glass requires high equipment cost and difficult process, which is not conducive to large-scale production, while the sol-gel method is relatively More economical preparation method. The traditional sol-gel process with high solid content and low shrinkage rate is suitable for the preparation of large-sized glass devices. Due to the influence of the mold processing size, it is impossible to directly produce micron-level fine optical structures.
此外,发明人将传统的低收缩率方案的溶胶凝胶工艺应用到大收缩率的方案设计中,发现会出现预料不到的凝胶过速、微结构变形等问题,难以获得满意的产品。In addition, the inventor applied the traditional low-shrinkage solution sol-gel process to the large-shrinkage solution design, and found that unexpected problems such as excessive gel speed and microstructure deformation would occur, making it difficult to obtain satisfactory products.
发明内容Summary of the invention
针对上述现有技术的高成本、工艺复杂、良品率低的缺陷,本发明提供一种微光学玻璃器件的制备方法,包括以下步骤:步骤一:获取二氧化硅分散液,将酸性溶液加入所述二氧化硅分散液,以调节所述二氧 化硅分散液的pH值至第一pH值,并搅拌;步骤二:将正硅酸乙酯加入所述二氧化硅分散液,并搅拌,得到溶胶,将碱性溶液加入所述溶胶,以调节所述溶胶的pH值至第二pH值,搅拌并静置;步骤三:将静置后的所述溶胶注入模具,陈化,得到湿凝胶;步骤四:将所述湿凝胶脱模,清洗、干燥,得到干凝胶;步骤五:将所述干凝胶烧结,得到微光学玻璃器件;其中,所述第二pH值的范围为3.0~4.0,所述微光学玻璃器件相对于所述湿凝胶的收缩率大于88%,所述二氧化硅分散液中所含的二氧化硅与所述正硅酸乙酯的摩尔比范围为3.8~5.4。In view of the high cost, complex process, and low yield of the prior art, the present invention provides a method for preparing a micro-optical glass device, which includes the following steps: Step 1: Obtain a silica dispersion, and add an acid solution to the The silica dispersion liquid to adjust the pH value of the silica dispersion liquid to the first pH value and stir; Step 2: adding ethyl orthosilicate to the silica dispersion liquid and stirring to obtain Sol, adding an alkaline solution to the sol to adjust the pH value of the sol to the second pH value, stirring and standing; Step 3: Injecting the standing sol into a mold, aging, and obtaining wet coagulation Glue; Step 4: demold the wet gel, wash and dry to obtain a dry gel; Step 5: sinter the dry gel to obtain a micro-optical glass device; wherein, the range of the second pH value Is 3.0 to 4.0, the shrinkage rate of the micro-optical glass device relative to the wet gel is greater than 88%, and the molar ratio of the silica contained in the silica dispersion to the ethyl orthosilicate The range is 3.8~5.4.
在一个实施方式中,在所述原料中,所述二氧化硅分散液所含的二氧化硅与所述正硅酸乙酯的摩尔比为3.8~4.6。In one embodiment, in the raw material, the molar ratio of silica contained in the silica dispersion to the ethyl orthosilicate is 3.8 to 4.6.
在一个实施方式中,原料中的二氧化硅固含量不大于21%,所述固含量是指所述二氧化硅分散液中所含的二氧化硅与所述正硅酸乙酯可水解产生的二氧化硅的总和占全部原料的质量百分比。In one embodiment, the solid content of silicon dioxide in the raw material is not more than 21%, and the solid content means that the silicon dioxide and the ethyl orthosilicate contained in the silicon dioxide dispersion can be hydrolyzed to produce The total amount of silica accounts for the mass percentage of all raw materials.
在一个实施方式中,在所述步骤一中,包括:获取预设摩尔体积的二氧化硅分散液原液,将所述二氧化硅分散液原液与去离子水混合,得到所述二氧化硅分散液,所述去离子水用于调节所述二氧化硅的固含量。In one embodiment, the step one includes: obtaining a silica dispersion stock solution with a preset molar volume, and mixing the silica dispersion stock solution with deionized water to obtain the silica dispersion The deionized water is used to adjust the solid content of the silica.
在一个实施方式中,所述第二pH值的范围为3.4~4.0。In one embodiment, the second pH value ranges from 3.4 to 4.0.
在一个实施方式中,在所述步骤一中,所述酸性溶液为盐酸溶液,所述第一pH值的范围为1.3~2.8。In one embodiment, in the step 1, the acidic solution is a hydrochloric acid solution, and the first pH value ranges from 1.3 to 2.8.
在一个实施方式中,所述模具为硅胶模具。In one embodiment, the mold is a silicone mold.
在一个实施方式中,在所述步骤五中,烧结温度不高于1200℃。In one embodiment, in the fifth step, the sintering temperature is not higher than 1200°C.
在一个实施方式中,在所述步骤四中,所述干燥包括第一干燥阶段和第二干燥阶段,所述第一干燥阶段温度至少低于所述第二干燥阶段温度100℃。In one embodiment, in the step four, the drying includes a first drying stage and a second drying stage, and the temperature of the first drying stage is at least 100° C. lower than the temperature of the second drying stage.
在一个实施方式中,所述微光学玻璃器件的最小微结构尺寸不大于1μm。In one embodiment, the smallest microstructure size of the micro-optical glass device is not greater than 1 μm.
与现有技术相比,本发明包括如下有益效果:大收缩率的溶胶凝胶制备光学玻璃器件,在凝胶阶段采用低于一般工艺的pH值,并选择合适的二氧化硅与正硅酸乙酯的比例,既保证了容易凝胶,又避免了凝胶速度过快,可以一次性获得具有精细结构的光学玻璃器件。Compared with the prior art, the present invention includes the following beneficial effects: a sol-gel with a large shrinkage ratio is used to prepare optical glass devices, a pH value lower than the general process is used in the gel stage, and suitable silica and orthosilicic acid are selected. The ratio of ethyl ester not only ensures easy gelation, but also avoids excessively fast gelation, and optical glass devices with fine structures can be obtained at one time.
附图说明Description of the drawings
图1为本发明的微光学玻璃器件的制备方法的流程示意图。Figure 1 is a schematic flow chart of the method for preparing the micro-optical glass device of the present invention.
具体实施方式Detailed ways
下面结合附图和实施方式对本发明实施例进行详细说明。The embodiments of the present invention will be described in detail below with reference to the accompanying drawings and embodiments.
在本发明中,主要的发明构思在于对溶胶凝胶法制备玻璃器件的两种二氧化硅源的配比及在该配比下的凝胶条件进行控制,从而获得大收缩率的制备。以气相二氧化硅粉末分散于水中得到的二氧化硅分散液具有减缓凝胶速度、避免正硅酸乙酯水解凝胶过快而导致开裂的功用,而凝胶过程中的pH值控制对控制凝胶速度影响巨大,本发明将两者结合,以解决在制备大收缩率玻璃器件过程中新遇到的微结构良率问题。In the present invention, the main inventive concept is to control the ratio of the two silica sources for preparing glass devices by the sol-gel method and the gel conditions under the ratio, so as to obtain a large shrinkage ratio. The silica dispersion liquid obtained by dispersing fumed silica powder in water has the function of slowing down the gel speed and avoiding the cracking caused by the too fast hydrolysis of the ethyl orthosilicate, and the pH value control during the gel process is very important for the control. The gel speed has a huge impact, and the present invention combines the two to solve the problem of microstructure yield newly encountered in the process of preparing glass devices with large shrinkage rates.
本发明所述的固含量,是指原料中的二氧化硅(包括正硅酸乙酯水解后的二氧化硅)占全部原料的质量百分比。The solid content in the present invention refers to the mass percentage of silicon dioxide in the raw materials (including silicon dioxide after the hydrolysis of ethyl orthosilicate) in the total raw materials.
请参见图1,为本发明的微光学玻璃器件的制备方法的流程示意图,包括:步骤一,获取二氧化硅分散液,并调节至第一pH值;步骤二,将二氧化硅分散液与正硅酸乙酯混合,并调节至第二pH值;步骤三,制备湿凝胶;步骤四,制备干凝胶;步骤五,烧结,得到微光学玻璃器件。下面对各个步骤进行详细描述。Please refer to Figure 1, which is a schematic flow chart of the method for preparing the micro-optical glass device of the present invention, including: step one, obtaining a silica dispersion liquid, and adjusting to a first pH; step two, combining the silica dispersion liquid with Ethyl orthosilicate is mixed and adjusted to the second pH value; step three, preparing wet gel; step four, preparing dry gel; step five, sintering, to obtain micro-optical glass device. Each step is described in detail below.
<步骤一><Step 1>
本步骤包括,获取二氧化硅分散液,将酸性溶液加入二氧化硅分散液,以调节二氧化硅分散液的pH值至第一pH值,并搅拌,最终得到预设pH值的二氧化硅分散液,作为第一二氧化硅源。This step includes obtaining a silica dispersion liquid, adding an acidic solution to the silica dispersion liquid to adjust the pH value of the silica dispersion liquid to a first pH value, and stirring, to finally obtain silica with a preset pH value The dispersion is used as the first silica source.
在本发明中,初始的二氧化硅分散液(即未调节pH值的)可以通过将气相二氧化硅与去离子水混合搅拌获得,通过磁力搅拌、均质机和/或超声分散,使得气相二氧化硅在水中分散均匀。而后,还要将二氧化硅分散液进行过滤,去除杂质和未被分散的团聚颗粒。In the present invention, the initial silica dispersion (that is, the pH value is not adjusted) can be obtained by mixing and stirring fumed silica and deionized water, and dispersing by magnetic stirring, homogenizer and/or ultrasonic, so that the gas phase Silica is evenly dispersed in water. Then, the silica dispersion is filtered to remove impurities and undispersed agglomerated particles.
本发明中的气相二氧化硅选择D50在20nm~150nm范围内的粒径尺寸,具有较大的比表面积。The fumed silica in the present invention selects a particle size with a D50 in the range of 20 nm to 150 nm, and has a larger specific surface area.
通常,要保证二氧化硅分散液的均匀性,需要较长时间的上述处理过程,导致每次生产的时间较长。因此,在本发明的一个实施方式中,事先大量配置预设摩尔体积的二氧化硅分散液原液,每次生产时并获取一定量的二氧化硅分散液原液,将其与去离子水混合稀释,其中,去离子水用于调节二氧化硅固含量,从而得到该生产批次的二氧化硅分散液。该技术方案使得对二氧化硅固含量的调节变得简单,而且减少了混合均匀所需的时间,不必每次过滤除杂,提高了生产效率,提高了不同批次生产中的原料稳定性。Generally, to ensure the uniformity of the silica dispersion liquid, a long time is required for the above-mentioned treatment process, resulting in a long time for each production. Therefore, in one embodiment of the present invention, a large amount of silica dispersion stock solution with a preset molar volume is prepared in advance, and a certain amount of silica dispersion stock solution is obtained during each production, and mixed and diluted with deionized water. Among them, deionized water is used to adjust the solid content of silica, so as to obtain the silica dispersion of the production batch. The technical solution makes the adjustment of the silica solid content simple, reduces the time required for uniform mixing, does not need to filter and remove impurities every time, improves production efficiency, and improves the stability of raw materials in different batches of production.
将酸性溶液加入二氧化硅分散液搅拌均匀,酸性溶液可以例如是稀盐酸溶液,使得二氧化硅分散液经调节pH值后为1.3~2.8。可以理解,酸性溶液也可以是其他用于调节pH值的酸性溶液。The acidic solution is added to the silica dispersion and stirred uniformly. The acidic solution can be, for example, a dilute hydrochloric acid solution, so that the silica dispersion is adjusted to a pH value of 1.3-2.8. It can be understood that the acidic solution may also be other acidic solutions for adjusting the pH value.
<步骤二><Step two>
获得酸性的二氧化硅分散液后,将正硅酸乙酯加入到该二氧化硅分散液中,并搅拌,正硅酸乙酯水解,得到溶胶,进一步将碱性溶液加入溶胶,以调节溶胶的pH值至第二pH值,搅拌并静置。在静置过程中,溶胶将开始逐渐形成凝胶,该过程不宜过长,只需短时间静置以排出搅拌过程中的气泡即可。After the acidic silica dispersion is obtained, ethyl orthosilicate is added to the silica dispersion and stirred, and the ethyl orthosilicate is hydrolyzed to obtain a sol, and an alkaline solution is further added to the sol to adjust the sol PH value to the second pH value, stir and let stand. During the standing process, the sol will gradually form a gel. The process should not be too long, and it only needs to stand for a short time to expel the bubbles during the stirring process.
在本发明的实施方式中,碱性溶液可以为氨水溶液,溶胶经调节pH值后,pH值上升,最终为3.0~4.0。可以理解,碱性溶液也可以是其他用于调节pH值的碱性溶液。In the embodiment of the present invention, the alkaline solution may be an aqueous ammonia solution. After the pH value of the sol is adjusted, the pH value increases, and finally is 3.0-4.0. It can be understood that the alkaline solution may also be other alkaline solutions for adjusting the pH value.
在本发明中,由于从步骤二到步骤三之间存在一个在原始容器(非模具)中静置的过程,而该过程对避免最终产品中有气泡至关重要,因此溶胶的凝胶化过程不能太快,否则难以将其在凝胶定型之前转移至模具中。发明人经过反复研究得出,自第二pH值超过4.0始,步骤三受明显影响,得到的湿凝胶的表面微结构不清晰。In the present invention, since there is a process of standing in the original container (not mold) from step 2 to step 3, and this process is very important to avoid bubbles in the final product, so the gelation process of the sol It should not be too fast, otherwise it will be difficult to transfer it to the mold before the gel is set. After repeated studies, the inventor has concluded that since the second pH value exceeds 4.0, step 3 is obviously affected, and the surface microstructure of the obtained wet gel is not clear.
在优选的实施方式中,第二pH值在最大值以内越大越好,第二pH值越小,凝胶难度越大,优选的范围为3.4~4.0。In a preferred embodiment, the larger the second pH value is within the maximum value, the better, the smaller the second pH value, the greater the difficulty of gelation, and the preferred range is 3.4-4.0.
在本发明中,制备大收缩率的微光学玻璃器件,为提高收缩率,采用降低二氧化硅固含量的方法,使得原料中的二氧化硅固含量不大于21%。以往的溶胶凝胶制备玻璃的方法中,普遍采用高固含量的原料配 比,通常至少在25%以上,该类制备方法难以实现微小光学结构的成型。In the present invention, to prepare a micro-optical glass device with a large shrinkage rate, in order to increase the shrinkage rate, a method of reducing the solid content of silica is adopted so that the solid content of silica in the raw material is not more than 21%. In the previous sol-gel method for preparing glass, a high solid content ratio of raw materials is generally used, usually at least 25% or more. This type of preparation method is difficult to achieve the formation of tiny optical structures.
<步骤三><Step Three>
将静置后的溶胶注入模具,陈化,得到湿凝胶。The static sol is poured into a mold and aged to obtain a wet gel.
在该步骤中,模具根据需要可以是各种形状、各种尺寸,从而可以得到各种形状、尺寸的玻璃光学器件。经陈化后,湿凝胶具有一定强度,可以从模具中脱模,为了便于脱模,本发明优选地采用硅胶模具,可以在硅胶模具一定的形变范围内将湿凝胶剥离出来。如果采用刚性模具,一方面可能损坏精细的光学表面结构,造成毛刺、裂痕,另一方面不易将湿凝胶脱出。In this step, the mold can be of various shapes and sizes as required, so that glass optical devices of various shapes and sizes can be obtained. After aging, the wet gel has a certain strength and can be demolded from the mold. In order to facilitate demolding, the present invention preferably adopts a silicone mold to peel off the wet gel within a certain deformation range of the silicone mold. If a rigid mold is used, on the one hand, it may damage the fine optical surface structure, causing burrs and cracks, and on the other hand, it is not easy to remove the wet gel.
<步骤四><Step Four>
将湿凝胶脱模,清洗、干燥,得到干凝胶。The wet gel is demolded, washed and dried to obtain a dry gel.
脱模后,得到带有转印精细结构的湿凝胶块。将该湿凝胶块可能存在一定的不均匀杂质,对其进行清洗,除去表面杂质,有利于得到透明度更高的产品。After demolding, a wet gel block with transfer fine structure is obtained. There may be certain uneven impurities in the wet gel block, and cleaning it to remove surface impurities is conducive to obtaining a product with higher transparency.
在对湿凝胶块进行干燥时,温度不宜过高,否则可能导致脱水过于激烈而导致样品开裂。When drying the wet gel block, the temperature should not be too high, otherwise it may cause excessive dehydration and cause the sample to crack.
干燥后,得到相对于湿凝胶块体积缩小的干凝胶块。该步骤是制备微光学玻璃器件过程中体积收缩的主要部分,收缩率很大。After drying, a dry gel block with a reduced volume relative to the wet gel block is obtained. This step is the main part of the volume shrinkage in the process of preparing the micro-optical glass device, and the shrinkage rate is very large.
在本发明的一个优选实施方式中,干燥步骤包括两步,即包括第一干燥阶段和第二干燥阶段。第一干燥阶段温度至少比第二干燥阶段温度低100℃,以避免在干燥过程中水从湿凝胶中剧烈脱离而导致开裂。具体地,在一个实施方式中,第一干燥阶段在空气气氛下进行,干燥温度为30℃~90℃;第二干燥阶段在无氧、无水汽的气氛下进行,干燥温度为150℃~500℃。In a preferred embodiment of the present invention, the drying step includes two steps, that is, it includes a first drying stage and a second drying stage. The temperature in the first drying stage is at least 100° C. lower than the temperature in the second drying stage to avoid violent separation of water from the wet gel during the drying process and causing cracking. Specifically, in one embodiment, the first drying stage is carried out in an air atmosphere, and the drying temperature is 30°C to 90°C; the second drying stage is carried out in an oxygen-free and moisture-free atmosphere, and the drying temperature is 150°C to 500°C. ℃.
<步骤五><Step 5>
将干凝胶烧结,得到微光学玻璃器件。该步骤中,样品得到第二次体积收缩,并由不透明转为透明玻璃器件。The dry gel is sintered to obtain a micro-optical glass device. In this step, the sample gets a second volume shrinkage, and changes from opaque to transparent glass device.
通常地,在现有技术的溶胶凝胶法制备光学玻璃的技术方案中,烧结需要在1200℃以上进行,发明人发现,高温下烧结会损坏光学玻璃器件的边缘、表面,使其轻微变形甚至开裂。在传统的较大尺寸的光学玻 璃器件中(如毫米级光学器件),这类表面缺陷影响不大,但是在微光学玻璃器件中,这会严重影响器件的光学性能。在本发明中,发明人发现,通过降低原料中二氧化硅的固含量,即使降低烧结温度也可以获得透明度高的光学器件。在本发明的优选实施方式中,烧结温度不高于1200℃,不但保护了玻璃表面的微光学结构不开裂,还能够降低低固含量下内部晶化、透明度下降的风险,提升了产品良率。此外,烧结温度的降低还能够降低能耗和生产成本。Generally, in the prior art technical solution for preparing optical glass by the sol-gel method, sintering needs to be performed at a temperature above 1200°C. The inventor found that sintering at high temperatures will damage the edges and surfaces of optical glass devices, causing them to slightly deform or even deform. Cracked. In traditional larger-sized optical glass devices (such as millimeter-level optical devices), such surface defects have little effect, but in micro-optical glass devices, this will seriously affect the optical performance of the device. In the present invention, the inventor found that by reducing the solid content of silica in the raw material, an optical device with high transparency can be obtained even if the sintering temperature is lowered. In the preferred embodiment of the present invention, the sintering temperature is not higher than 1200°C, which not only protects the micro-optical structure of the glass surface from cracking, but also reduces the risk of internal crystallization and decreased transparency at low solid content, and improves the product yield. . In addition, the reduction of sintering temperature can also reduce energy consumption and production costs.
以上,对制备步骤进行了详细说明,下面请参考具体实施例,为便于对各技术方案效果进行对比,选择相同实验条件下的不同第二pH值,以及不同的二氧化硅分散液所含的二氧化硅与正硅酸乙酯的摩尔比。Above, the preparation steps are described in detail. Please refer to the specific examples below. In order to facilitate the comparison of the effects of various technical solutions, choose different second pH values under the same experimental conditions and different silica dispersions. The molar ratio of silica to tetraethyl orthosilicate.
实施例Example
首先称取气相二氧化硅颗粒和去离子水,混合搅拌,使用均质机分散均匀;加入稀盐酸,调节pH=2,搅拌后,加入正硅酸乙酯,搅拌形成溶胶溶液,接着加入氨水调节溶胶为第二pH值,搅拌后静置,注入带有微结构模具中,等待一定时间后凝胶,再静置预设时间后脱模。First, weigh the fumed silica particles and deionized water, mix and stir, use a homogenizer to disperse evenly; add dilute hydrochloric acid, adjust pH=2, after stirring, add ethyl orthosilicate, stir to form a sol solution, and then add ammonia Adjust the sol to the second pH value, stir and then stand still, pour it into a mold with a microstructure, wait for a certain period of time to gel, and then leave it to stand for a preset time before demolding.
将上述带有微结构的湿凝胶放入纯去离子水中,进行循环水洗,水洗后放入温度为45℃恒温恒湿箱中进行第一阶段干燥,而后在200℃氮气气氛下进行第二阶段干燥,样品干燥后经过1100℃保温12h烧结得到具有微结构的光学元件。Put the above-mentioned wet gel with microstructure in pure deionized water, wash it with circulating water, after washing, put it into a constant temperature and humidity box at 45℃ for the first stage of drying, and then carry out the second stage in a nitrogen atmosphere at 200℃ Staged drying. After the sample is dried, it is sintered at 1100°C for 12 hours to obtain an optical element with a microstructure.
各实施例、对比例的数据表见下图,其中,固含量的解释参见上文说明;比例是气相二氧化硅颗粒或二氧化硅分散液原液中含有的二氧化硅(SiO 2)的物质的量与正硅酸乙酯(TEOS)的物质的量的比n SiO2/n TEOS;收缩率为烧结后的玻璃器件相对于脱模后的凝胶的体积收缩率,可通过阿基米德法测量;良率是指开裂、划痕、脏污、气泡以及透过率极低的情况为不良品。 The data table of each example and comparative example is shown in the figure below, in which, the explanation of the solid content is referred to the above description; the ratio is the substance of silica (SiO 2) contained in the fumed silica particles or silica dispersion stock solution The ratio of the amount of TEOS to the amount of TEOS n SiO2 /n TEOS; the shrinkage rate is the volume shrinkage rate of the sintered glass device relative to the gel after demolding, which can be passed through Archimedes Method measurement; Yield rate refers to defective products with cracks, scratches, dirt, bubbles, and extremely low transmittance.
Figure PCTCN2020135095-appb-000001
Figure PCTCN2020135095-appb-000001
Figure PCTCN2020135095-appb-000002
Figure PCTCN2020135095-appb-000002
在本发明中,对第二pH值和n SiO2/n TEOS的研究都是基于大收缩率的背景下,本发明制得的微光学玻璃器件相对于湿凝胶的收缩率大于88%,大收缩率才会有微光学结构成型存在的形状完整等问题。 In the present invention, the research on the second pH value and n SiO2 /n TEOS is based on the background of large shrinkage rate. The shrinkage rate of the micro-optical glass device prepared by the present invention is greater than 88% relative to the wet gel. The shrinkage will cause problems such as the complete shape of the micro-optical structure molding.
在本发明中,溶胶粒子的等电点是pH=2,溶胶粒子表面无法吸附电荷,缩聚反应进行的比较慢,过渡态难以形成,体系胶凝时间较长;当pH>2时,溶胶粒子表面可以吸附一定数量的OH-,通过分子振动及化学键断裂,将产生SiO-,它可以进攻其他溶胶分子的中心Si原子,发生缩聚反应,其缩聚反应机理是亲核反应机理。发明人经反复实验发现,当第二pH值低于3.0时,凝胶时间漫长,即使得到了凝胶,制得的样品也极易开裂;随着pH值的升高,凝胶时间缩短,凝胶后的样品经干燥、烧结得到的玻璃器件的良率也逐渐提高;但是,当pH值超过4.0后,凝胶速度过快,不利于微结构的形成。在本发明中,优选地微光学器件的最小微结构尺寸不大于1μm,第二pH值超过4.0将难以形成该微结构。In the present invention, the isoelectric point of the sol particles is pH=2, the surface of the sol particles cannot absorb charges, the polycondensation reaction progresses relatively slowly, the transition state is difficult to form, and the system gel time is longer; when the pH>2, the sol particles The surface can absorb a certain amount of OH-, and through molecular vibration and chemical bond breakage, SiO- will be produced, which can attack the central Si atom of other sol molecules and cause condensation reaction. The condensation reaction mechanism is a nucleophilic reaction mechanism. The inventor found through repeated experiments that when the second pH value is lower than 3.0, the gel time is long, and even if the gel is obtained, the prepared sample is extremely easy to crack; as the pH value increases, the gel time is shortened, The yield rate of the glass device obtained by drying and sintering the sample after the gel is gradually improved; however, when the pH value exceeds 4.0, the gel speed is too fast, which is not conducive to the formation of microstructure. In the present invention, it is preferable that the minimum microstructure size of the micro-optical device is not greater than 1 μm, and it is difficult to form the microstructure if the second pH value exceeds 4.0.
在相同的第二pH值下,实验数据表明,原理中的二氧化硅分散液的二氧化硅不宜占比过大,否则会导致良率下降。Under the same second pH value, the experimental data shows that the silica dispersion in the principle should not account for too much silica, otherwise the yield will decrease.
正硅酸乙酯(TEOS)有助于凝胶过程,如果仅采用二氧化硅分散液作为二氧化硅源,其形成凝胶的过程极其缓慢,不能够应用于产品量产中,随着增加正硅酸乙酯的量,所需的凝胶时间逐渐缩短。经发明人研究,二氧化硅分散液所含的二氧化硅与正硅酸乙酯的摩尔比n SiO2/n TEOS在5.4以下时可满足量产要求。 Ethyl orthosilicate (TEOS) contributes to the gel process. If only silica dispersion is used as the silica source, the gel formation process is extremely slow and cannot be used in mass production of products. The amount of ethyl orthosilicate, the required gel time is gradually shortened. According to the inventor's research, the molar ratio n SiO 2 /n TEOS of silicon dioxide to tetraethyl orthosilicate contained in the silicon dioxide dispersion liquid is below 5.4, which can meet the mass production requirements.
然而过多的正硅酸乙酯可能导致凝胶收缩时开裂。从表中数据看出,在同样的第二pH值下,随着n SiO2/n TEOS的减小,良率先升后降,当n SiO2/n TEOS达到低至2.8时,良率已降低至40%,再小的比值的经济价值不大。 However, too much tetraethyl orthosilicate may cause the gel to crack when it shrinks. Seen from the data in the table, a second at the same pH value, with n SiO2 / n decrease of TEOS, good after elevating the lead, when n SiO2 / n TEOS as low as 2.8, the yield has decreased to 40%, the smaller the ratio has little economic value.
在本发明中,并非要求良率100%的方案才被采纳,需要综合考虑良率和生产时间,较高的良率往往代表更长的凝胶时间,只要在单位时间内的良品数量较高即可。In the present invention, the solution that does not require a 100% yield rate is adopted. The yield rate and production time need to be considered comprehensively. A higher yield rate often represents a longer gel time, as long as the number of good products per unit time is higher. That's it.
因此,在本发明中,二氧化硅分散液所含的二氧化硅与正硅酸乙酯的摩尔比为3.8~5.4。优选地,二氧化硅分散液所含的二氧化硅与正硅酸乙酯的摩尔比为3.8~4.6。Therefore, in the present invention, the molar ratio of silica to tetraethyl orthosilicate contained in the silica dispersion is 3.8 to 5.4. Preferably, the molar ratio of silica to tetraethyl orthosilicate contained in the silica dispersion is 3.8 to 4.6.
本说明书中各个实施例采用递进的方式描述,每个实施例重点说明的都是与其他实施例的不同之处,各个实施例之间相同相似部分互相参见即可。The various embodiments in this specification are described in a progressive manner. Each embodiment focuses on the differences from other embodiments, and the same or similar parts between the various embodiments can be referred to each other.
以上所述仅为本发明的实施方式,并非因此限制本发明的专利范围,凡是利用本发明说明书及附图内容所作的等效结构或等效流程变换,或直接或间接运用在其他相关的技术领域,均同理包括在本发明的专利保护范围内。The above are only the embodiments of the present invention, and do not limit the scope of the present invention. Any equivalent structure or equivalent process transformation made by using the contents of the description and drawings of the present invention, or directly or indirectly applied to other related technologies In the same way, all fields are included in the scope of patent protection of the present invention.

Claims (10)

  1. 一种微光学玻璃器件的制备方法,其特征在于,包括以下步骤:A method for preparing a micro-optical glass device is characterized in that it comprises the following steps:
    步骤一:获取二氧化硅分散液,将酸性溶液加入所述二氧化硅分散液,以调节所述二氧化硅分散液的pH值至第一pH值,并搅拌;Step 1: Obtain a silica dispersion liquid, add an acidic solution to the silica dispersion liquid to adjust the pH value of the silica dispersion liquid to the first pH value, and stir;
    步骤二:将正硅酸乙酯加入所述二氧化硅分散液,并搅拌,得到溶胶,将碱性溶液加入所述溶胶,以调节所述溶胶的pH值至第二pH值,搅拌并静置;Step 2: Add ethyl orthosilicate to the silica dispersion liquid and stir to obtain a sol, add an alkaline solution to the sol to adjust the pH value of the sol to the second pH value, stir and stand still Set
    步骤三:将静置后的所述溶胶注入模具,陈化,得到湿凝胶;Step 3: Inject the static sol into a mold and age to obtain a wet gel;
    步骤四:将所述湿凝胶脱模,清洗、干燥,得到干凝胶;Step 4: demoulding the wet gel, washing and drying, to obtain a dry gel;
    步骤五:将所述干凝胶烧结,得到微光学玻璃器件;Step 5: Sintering the dry gel to obtain a micro-optical glass device;
    其中,所述第二pH值的范围为3.0~4.0,所述微光学玻璃器件相对于所述湿凝胶的收缩率大于88%,所述二氧化硅分散液中所含的二氧化硅与所述正硅酸乙酯的摩尔比范围为3.8~5.4。Wherein, the second pH value ranges from 3.0 to 4.0, the shrinkage rate of the micro-optical glass device relative to the wet gel is greater than 88%, and the silica contained in the silica dispersion is more than The molar ratio of the ethyl orthosilicate ranges from 3.8 to 5.4.
  2. 根据权利要求1所述的微光学玻璃器件的制备方法,其特征在于,在所述原料中,所述二氧化硅分散液所含的二氧化硅与所述正硅酸乙酯的摩尔比为3.8~4.6。The method for preparing a micro-optical glass device according to claim 1, wherein, in the raw material, the molar ratio of the silica contained in the silica dispersion to the ethyl orthosilicate is 3.8~4.6.
  3. 根据权利要求1所述的微光学玻璃器件的制备方法,其特征在于,原料中的二氧化硅固含量不大于21%,所述固含量是指所述二氧化硅分散液中所含的二氧化硅与所述正硅酸乙酯可水解产生的二氧化硅的总和占全部原料的质量百分比。The method for preparing a micro-optical glass device according to claim 1, wherein the solid content of silicon dioxide in the raw material is not more than 21%, and the solid content refers to the silicon dioxide contained in the silicon dioxide dispersion. The sum of silicon oxide and silicon dioxide produced by the hydrolysis of the ethyl orthosilicate accounts for the mass percentage of all raw materials.
  4. 根据权利要求3所述的微光学玻璃器件的制备方法,其特征在于,在所述步骤一中,包括:获取预设摩尔体积的二氧化硅分散液原液,将所述二氧化硅分散液原液与去离子水混合,得到所述二氧化硅分散液,所述去离子水用于调节所述二氧化硅的固含量。The method for preparing a micro-optical glass device according to claim 3, characterized in that, in the step one, it comprises: obtaining a silica dispersion stock solution of a preset molar volume, and combining the silica dispersion stock solution It is mixed with deionized water to obtain the silica dispersion, and the deionized water is used to adjust the solid content of the silica.
  5. 根据权利要求1~4中任一项所述的微光学玻璃器件的制备方法,其特征在于,所述第二pH值的范围为3.4~4.0。The method for preparing a micro-optical glass device according to any one of claims 1 to 4, wherein the second pH value ranges from 3.4 to 4.0.
  6. 根据权利要求1~4中任一项所述的微光学玻璃器件的制备方法,其特征在于,在所述步骤一中,所述酸性溶液为盐酸溶液,所述第一pH值的范围为1.3~2.8。The method for preparing a micro-optical glass device according to any one of claims 1 to 4, wherein, in the step 1, the acidic solution is a hydrochloric acid solution, and the first pH value is in the range of 1.3 ~2.8.
  7. 根据权利要求1~4中任一项所述的微光学玻璃器件的制备方法,其特征在于,所述模具为硅胶模具。The method for preparing a micro-optical glass device according to any one of claims 1 to 4, wherein the mold is a silicone mold.
  8. 根据权利要求1~4中任一项所述的微光学玻璃器件的制备方法,其特征在于,在所述步骤五中,烧结温度不高于1200℃。The method for preparing a micro-optical glass device according to any one of claims 1 to 4, characterized in that, in the fifth step, the sintering temperature is not higher than 1200°C.
  9. 根据权利要求1~4中任一项所述的微光学玻璃器件的制备方法,其特征在于,在所述步骤四中,所述干燥包括第一干燥阶段和第二干燥阶段,所述第一干燥阶段温度至少低于所述第二干燥阶段温度100℃。The method for preparing a micro-optical glass device according to any one of claims 1 to 4, characterized in that, in the step four, the drying includes a first drying stage and a second drying stage, and the first drying stage The temperature of the drying stage is at least 100°C lower than the temperature of the second drying stage.
  10. 根据权利要求1~4中任一项所述的微光学玻璃器件的制备方法,其特征在于,所述微光学玻璃器件的最小微结构尺寸不大于1μm。The method for manufacturing a micro-optical glass device according to any one of claims 1 to 4, wherein the smallest microstructure size of the micro-optical glass device is not greater than 1 μm.
PCT/CN2020/135095 2019-12-31 2020-12-10 Method for preparing micro optical glass device WO2021135881A1 (en)

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