CN102826736A - Method for preparing hollow glass bead by using glass powder process - Google Patents
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Abstract
本发明公开一种玻璃粉末法制备空心玻璃微珠的方法,包括配料、熔融、粉碎、空心球化、收集、筛选、检验,所述粉碎步骤操作如下:熔化后的玻璃液在2MPa以上高压气体作用下通过多孔喷嘴喷出,使之形成向下溅落的熔融玻璃液滴,熔融玻璃液滴在下落过程中与高速旋转的转鼓表面碰撞,转鼓内通入循环水冷却,玻璃液滴在重力、离心力、溅射力的共同作用下形成粒径在1~100微米之间的玻璃颗粒;本发明的创新点是采用一种新的离心粉碎代替原生产工艺中水碎→烘干→粗碎→细碎的过程,简化了生产工艺,降低能耗,减少设备和人员成本,操作与质量易于控制;本发明可降低生产成本14~20%,提高抗压强度4.8~15%。The invention discloses a method for preparing hollow glass microspheres by a glass powder method, which includes batching, melting, pulverizing, hollow spheroidizing, collecting, screening, and testing. Under the action, it is sprayed through the porous nozzle to form molten glass droplets splashing downward. The molten glass droplets collide with the surface of the high-speed rotating drum during the falling process. Under the joint action of gravity, centrifugal force and sputtering force, glass particles with a particle size between 1 and 100 microns are formed; the innovation of this invention is to use a new centrifugal crushing instead of water crushing→drying→coarse crushing in the original production process. The process of crushing→fine crushing simplifies the production process, reduces energy consumption, reduces equipment and personnel costs, and is easy to control operation and quality; the invention can reduce production costs by 14-20% and increase compressive strength by 4.8-15%.
Description
技术领域: Technical field:
本发明涉及空心玻璃微珠的生产工艺,更具体的说,涉及一种玻璃粉末法制备空心玻璃微珠的方法。 The invention relates to a production process of hollow glass microspheres, and more specifically, relates to a method for preparing hollow glass microspheres by a glass powder method.
背景技术: Background technique:
空心玻璃微珠是一种中空的、内含一种或几种惰性气体的球形玻璃粉体,粒径分布从几个微米到几百个微米之间。独特的结构使之具备密度低、流动性好、导热系数低、抗压强度高、化学稳定性好的特点,目前已经应用在航空航天、石油开采、深海浮体材料、乳化炸药、高级绝缘材料、墙体隔热防火材料等军事、民用以及高科技领域。 Hollow glass microspheres are hollow spherical glass powders containing one or several inert gases, with a particle size distribution ranging from a few microns to hundreds of microns. The unique structure makes it have the characteristics of low density, good fluidity, low thermal conductivity, high compressive strength, and good chemical stability. It has been used in aerospace, oil exploration, deep-sea floating body materials, emulsion explosives, advanced insulation materials, Military, civilian and high-tech fields such as wall heat insulation and fireproof materials.
空心玻璃微珠的制备方法主要有干燥凝胶法、液滴法和玻璃粉末法,由于制备方法的限制,干燥凝胶法和液滴法制备的空心玻璃微珠强度都比较低,高端空心玻璃微珠的生产一般采用玻璃粉末法。 The preparation methods of hollow glass microspheres mainly include dry gel method, liquid drop method and glass powder method. Due to the limitation of preparation methods, the strength of hollow glass microspheres prepared by dry gel method and liquid drop method is relatively low, and high-end hollow glass The production of microbeads generally adopts the glass powder method.
玻璃粉末法生产工艺过程主要是:1配料→2熔化→3水碎→4烘干→5粗碎→6细碎→7空心球化→8收集→9筛选→10检验,配料熔化是根据要求配制不同类型的产品,空心球化是产品成型的必经过程,是目前较为成熟和稳定的工艺,从工业化的角度考虑,3水碎→4烘干→5粗碎→6细碎的操作过程相对繁琐,生产工艺复杂,设备多,能耗高,效率低,增加产品的不可控性。该段工艺具体过程为:首先将熔化好的玻璃液从熔窑中缓缓倒入通入冷水的水槽中通过水淬急冷将玻璃液变为玻璃碎,然后将其捞出烘干并通过对辊破碎机将其破碎为2毫米以下的玻璃碎,符合标准的玻璃碎送入气流磨中,粉碎为1~100微米的玻璃粉末。破碎过程中由于铁等杂质的引入导致玻璃微珠成分的改变、降低了空心玻璃微珠性能指标,同时带来噪音和粉尘污染;由于能源和人力成本的投入加大了生产成本,由于控制节点的增加也给空心玻璃微珠的质量控制增加了难度。 The production process of the glass powder method is mainly: 1 batching → 2 melting → 3 water crushing → 4 drying → 5 coarse crushing → 6 fine crushing → 7 hollow spheroidization → 8 collection → 9 screening → 10 inspection, the melting of ingredients is prepared according to requirements For different types of products, hollow spheroidization is a necessary process for product molding. It is a relatively mature and stable process at present. From the perspective of industrialization, the operation process of 3 water crushing → 4 drying → 5 coarse crushing → 6 fine crushing is relatively cumbersome , the production process is complicated, the equipment is many, the energy consumption is high, the efficiency is low, and the uncontrollability of the product is increased. The specific process of this section of the process is as follows: firstly, slowly pour the molten glass from the melting furnace into a water tank filled with cold water, and through water quenching and rapid cooling, the molten glass will be turned into broken glass, and then it will be taken out and dried and passed through the The roller crusher crushes it into glass fragments below 2 mm, and the standard glass fragments are sent to the jet mill to be crushed into glass powders of 1-100 microns. During the crushing process, the introduction of impurities such as iron leads to changes in the composition of the glass beads, which reduces the performance indicators of the hollow glass beads and brings noise and dust pollution; the input of energy and labor costs increases the production cost, and the control nodes The increase also increases the difficulty to the quality control of hollow glass microspheres.
发明内容 Contents of the invention
本发明的目的在于提供一种易于操作和控制的玻璃粉末法制备空心玻璃微珠的方法,生产成本降低14~20%,抗压强度提高4.8~15%。 The object of the present invention is to provide an easy-to-operate and control method for preparing hollow glass microspheres by glass powder method, which reduces production cost by 14-20% and increases compressive strength by 4.8-15%.
本发明的目的是通过对制备工艺中粉碎步骤进行如下改进实现的,一种玻璃粉末法制备空心玻璃微珠的方法,包括配料、熔融、粉碎、空心球化、收集、筛选、检验,本发明的创新点是将现有生产工艺中水碎→烘干→粗碎→细碎的过程简化为离心粉碎一步完成,所述粉碎步骤操作如下:熔化后的玻璃液在2MPa以上高压气体作用下通过多孔喷嘴喷出,使之形成向下溅落的熔融玻璃液滴,熔融玻璃液滴在下落过程中与高速旋转的转鼓表面碰撞,转鼓内通入循环水冷却,玻璃液滴在重力、离心力、溅射力的共同作用下形成粒径在1~100微米之间的玻璃颗粒并甩入粉料收集仓内。 The object of the present invention is achieved by improving the pulverizing step in the preparation process as follows, a method for preparing hollow glass microspheres by glass powder method, including batching, melting, pulverizing, hollow spheroidizing, collecting, screening, testing, the present invention The innovative point is to simplify the process of water crushing→drying→coarse crushing→fine crushing in the existing production process to centrifugal crushing in one step. The nozzle is ejected to form molten glass droplets splashing downward. The molten glass droplets collide with the surface of the high-speed rotating drum during the falling process. The circulating water is passed into the drum to cool. Under the joint action of sputtering force, glass particles with a particle size between 1 and 100 microns are formed and thrown into the powder collection bin.
本发明进一步技术方案是,所述玻璃液滴形成粒径的大小通过调节转鼓转速与喷射气体的压力控制。 The further technical solution of the present invention is that the particle size of the glass droplets formed is controlled by adjusting the rotational speed of the drum and the pressure of the injection gas.
本发明针对玻璃粉末法空心玻璃微珠生产工艺进行改进,采用一种新的离心粉碎代替原生产工艺中水碎→烘干→粗碎→细碎的过程,简化了生产工艺,降低能耗,减少设备和人员成本,操作与质量易于控制,水淬效果也更好;本发明可降低生产成本14~20%,提高抗压强度4.8~15%。 The invention improves the production process of hollow glass microspheres by glass powder method, adopts a new centrifugal crushing method to replace the process of water crushing → drying → coarse crushing → fine crushing in the original production process, simplifies the production process, reduces energy consumption, reduces Equipment and personnel costs, operation and quality are easy to control, and the water quenching effect is better; the invention can reduce the production cost by 14-20%, and increase the compressive strength by 4.8-15%.
具体实施方式 Detailed ways
实施例1 Example 1
采用产品密度为0.25 g/cm3的玻璃配方配置玻璃原料,将配好并混合均匀的玻璃原料放入窑炉中进行熔融,熔制温度1500℃~1600℃,熔制时间为1~3小时,熔融玻璃液在2.4Mpa的高压气体作用下通过多孔喷嘴向下喷出,形成快速向下溅射出的高速玻璃液滴,并在下落过程中与900r/min的高速转鼓表面碰撞,玻璃液滴在重力、离心力、溅射力的共同作用下甩成中位粒径在15微米左右的玻璃粉末。将玻璃粉末与空气混合喷入成珠炉,在1580℃的温度场内迅速空心球化。空心球化后的粉体主要通过旋风除尘器收集,剩余的超细粉体通过布袋收尘器收集。收集到的粉体利用空心玻璃微珠漂选装置分选,将空心玻璃微珠与玻璃微珠分开,同时烘干分级,生产出密度为0.25±0.02g/cm3,抗压强度9Mp,漂浮率≥98%的空心玻璃微珠,抗压强度提高12.5%,生产成本降低19%。 Use a glass formula with a product density of 0.25 g/ cm3 to configure glass raw materials, put the prepared and uniformly mixed glass raw materials into a furnace for melting, the melting temperature is 1500 ° C ~ 1600 ° C, and the melting time is 1 ~ 3 hours , the molten glass is sprayed downward through the porous nozzle under the action of 2.4Mpa high-pressure gas, forming high-speed glass droplets that sputter downward rapidly, and collide with the surface of the 900r/min high-speed drum during the falling process. The drops are thrown into glass powder with a median particle size of about 15 microns under the joint action of gravity, centrifugal force and sputtering force. The glass powder is mixed with air and sprayed into the beading furnace, and rapidly hollowed into spheres in a temperature field of 1580°C. The hollow spheroidized powder is mainly collected by the cyclone dust collector, and the remaining ultrafine powder is collected by the bag filter. The collected powder is sorted by the hollow glass microsphere floating separation device, the hollow glass microsphere is separated from the glass microsphere, and dried and classified at the same time to produce a density of 0.25±0.02g/cm 3 , a compressive strength of 9Mp, and a floating Hollow glass microspheres with an efficiency ≥ 98%, the compressive strength is increased by 12.5%, and the production cost is reduced by 19%.
实施例2 Example 2
采用产品密度为0.4g/cm3的玻璃配方配置玻璃原料,将配好并混合均匀的玻璃原料放入窑炉中进行熔融,熔制温度1480~1580℃,熔制时间为1~3小时,熔融玻璃液在2.2Mpa的高压气体作用下通过多孔喷嘴向下喷出,形成快速向下溅射出的高速玻璃液滴,并在下落过程中与800r/min的高速转鼓表面碰撞,玻璃液滴在重力、离心力、溅射力的共同作用下甩成中位粒径在20微米左右的玻璃粉末。将玻璃粉末与空气混合喷入成珠炉,在1540℃的温度场内迅速空心球化。空心球化后的粉体主要通过旋风除尘器收集,剩余的超细粉体通过布袋收尘器收集。收集到的粉体利用空心玻璃微珠漂选装置分选,将空心玻璃微珠与玻璃微珠分开,同时烘干分级,生产出密度为0.4±0.02g/cm3,抗压强度40 Mp,漂浮率≥95%的空心玻璃微珠,抗压强度提高11.1%,生产成本可降低17%。 Use a glass formula with a product density of 0.4g/ cm3 to configure glass raw materials, put the prepared and uniformly mixed glass raw materials into a furnace for melting, the melting temperature is 1480-1580°C, and the melting time is 1-3 hours. The molten glass is sprayed downward through the porous nozzle under the action of 2.2Mpa high-pressure gas, forming high-speed glass droplets sputtered downward rapidly, and colliding with the surface of the 800r/min high-speed drum during the falling process, the glass droplets Under the joint action of gravity, centrifugal force and sputtering force, it is thrown into glass powder with a median particle size of about 20 microns. The glass powder is mixed with air and sprayed into the beading furnace, and is rapidly hollowed into spheres in a temperature field of 1540°C. The hollow spheroidized powder is mainly collected by the cyclone dust collector, and the remaining ultrafine powder is collected by the bag filter. The collected powder is sorted by the hollow glass microsphere drifting device, and the hollow glass microsphere is separated from the glass microsphere, and is dried and classified at the same time to produce a density of 0.4±0.02g/cm 3 and a compressive strength of 40 Mp. Hollow glass microspheres with a floating rate ≥ 95% can increase the compressive strength by 11.1% and reduce production costs by 17%.
实施例3 Example 3
采用产品密度为0.7g/cm3的玻璃配方配置玻璃原料,将配好并混合均匀的玻璃原料放入窑炉中进行熔融,熔制温度1450~1550℃,熔制时间为1~3小时,熔融玻璃液在2.1Mpa的高压气体作用下通过多孔喷嘴向下喷出,形成快速向下溅射出的高速玻璃液滴,并在下落过程中与700r/min的高速转鼓表面碰撞,玻璃液滴在重力、离心力、溅射力的共同作用下甩成中位粒径在25微米左右的玻璃粉末。将玻璃粉末与空气混合喷入成珠炉,在1500℃的温度场内迅速空心球化。空心球化后的粉体主要通过旋风除尘器收集,剩余的超细粉体通过布袋收尘器收集。收集到的粉体利用空心玻璃微珠漂选装置分选,将空心玻璃微珠与玻璃微珠分开,同时烘干分级,生产出密度为0.7±0.02g/cm3,抗压强度131 Mp,漂浮率≥96%的空心玻璃微珠,抗压强度提高5%,生产成本降低14%。 Use a glass formula with a product density of 0.7g/ cm3 to configure glass raw materials, put the prepared and uniformly mixed glass raw materials into a furnace for melting, the melting temperature is 1450-1550 °C, and the melting time is 1-3 hours. The molten glass is sprayed downward through the porous nozzle under the action of 2.1Mpa high-pressure gas, forming high-speed glass droplets sputtered downward rapidly, and colliding with the surface of the 700r/min high-speed drum during the falling process, the glass droplets Under the joint action of gravity, centrifugal force and sputtering force, it is thrown into glass powder with a median particle size of about 25 microns. The glass powder is mixed with air and sprayed into the beading furnace, and rapidly hollowed into spheres in a temperature field of 1500°C. The hollow spheroidized powder is mainly collected by the cyclone dust collector, and the remaining ultrafine powder is collected by the bag filter. The collected powder is sorted by the hollow glass microsphere drifting device, and the hollow glass microsphere is separated from the glass microsphere. At the same time, it is dried and classified to produce a density of 0.7±0.02g/cm 3 and a compressive strength of 131 Mp. Hollow glass microspheres with a floating rate ≥ 96% can increase the compressive strength by 5% and reduce the production cost by 14%.
应当指出的是所谓抗压强度指的是对空心玻璃微珠施加经由气体或液体传导的等静压力,当空心玻璃微珠破裂10%(体积比)时对应的强度为其抗压强度。具体数据对比可见表一。三个不同配方空心玻璃微珠的抗压强度、密度及成本分析。 It should be pointed out that the so-called compressive strength refers to the isostatic pressure applied to the hollow glass microspheres via gas or liquid conduction. When the hollow glass microspheres are broken by 10% (volume ratio), the corresponding strength is its compressive strength. The specific data comparison can be seen in Table 1. Compressive strength, density and cost analysis of hollow glass microspheres with three different formulations.
表一 Table I
以上所述,仅是本发明的较佳实施例而已,并非对本发明作任何形式上的限制;任何熟悉本领域的技术人员,在不脱离本发明技术方案范围情况下,都可利用上述揭示的方法和技术内容对本发明技术方案做出许多可能的变动和修饰,或修改为等同变化的等效实施例。因此,凡是未脱离本发明技术方案的内容,依据本发明的技术实质对以上实施例所做的任何简单修改、等同替换、等效变化及修饰,均仍属于本发明技术方案保护的范围内。 The above is only a preferred embodiment of the present invention, and is not intended to limit the present invention in any form; any person skilled in the art can use the above disclosure without departing from the scope of the technical solution of the present invention. Methods and Technical Contents Many possible changes and modifications are made to the technical solution of the present invention, or modified into equivalent embodiments with equivalent changes. Therefore, any simple modifications, equivalent replacements, equivalent changes and modifications made to the above embodiments according to the technical essence of the present invention, which do not deviate from the technical solutions of the present invention, still fall within the protection scope of the technical solutions of the present invention.
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| 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 |
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| 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 |
| CN115925239A (en) * | 2022-12-15 | 2023-04-07 | 李勇 | A kind of hollow glass microsphere for high strength and preparation method thereof |
| 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 |
| CN117602821A (en) * | 2023-10-26 | 2024-02-27 | 中钢集团马鞍山矿山研究总院股份有限公司 | Method for preparing hollow glass microsphere precursor using hollow glass microsphere by-products as raw materials |
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| 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 microspheres |
| CN108609843B (en) * | 2018-04-20 | 2021-07-27 | 郭宝华 | Device and method for producing flaky material by using mineral raw material |
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| CN115925239A (en) * | 2022-12-15 | 2023-04-07 | 李勇 | A kind of hollow glass microsphere for high strength and preparation method thereof |
| 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 |
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