CN107459260A - It is a kind of using flyash as glass fibre of primary raw material and preparation method thereof - Google Patents
It is a kind of using flyash as glass fibre of primary raw material and preparation method thereof Download PDFInfo
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- CN107459260A CN107459260A CN201710572450.1A CN201710572450A CN107459260A CN 107459260 A CN107459260 A CN 107459260A CN 201710572450 A CN201710572450 A CN 201710572450A CN 107459260 A CN107459260 A CN 107459260A
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- fly ash
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- 239000010881 fly ash Substances 0.000 title claims abstract description 68
- 239000003365 glass fiber Substances 0.000 title claims abstract description 59
- 239000002994 raw material Substances 0.000 title claims abstract description 34
- 238000002360 preparation method Methods 0.000 title claims abstract description 6
- 239000011521 glass Substances 0.000 claims abstract description 31
- 239000000203 mixture Substances 0.000 claims abstract description 25
- 239000006004 Quartz sand Substances 0.000 claims abstract description 11
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229910021532 Calcite Inorganic materials 0.000 claims abstract description 9
- 239000010459 dolomite Substances 0.000 claims abstract description 8
- 229910000514 dolomite Inorganic materials 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims abstract description 7
- 238000010791 quenching Methods 0.000 claims abstract description 7
- 230000000171 quenching effect Effects 0.000 claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000000654 additive Substances 0.000 claims abstract description 5
- 239000004615 ingredient Substances 0.000 claims abstract description 5
- 238000005491 wire drawing Methods 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 15
- 238000002844 melting Methods 0.000 claims description 12
- 230000008018 melting Effects 0.000 claims description 12
- 230000008569 process Effects 0.000 claims description 8
- 239000003245 coal Substances 0.000 claims description 7
- 238000001035 drying Methods 0.000 claims description 6
- 239000006060 molten glass Substances 0.000 claims description 6
- 238000004513 sizing Methods 0.000 claims description 6
- 239000008395 clarifying agent Substances 0.000 claims description 5
- 239000010446 mirabilite Substances 0.000 claims description 5
- RSIJVJUOQBWMIM-UHFFFAOYSA-L sodium sulfate decahydrate Chemical compound O.O.O.O.O.O.O.O.O.O.[Na+].[Na+].[O-]S([O-])(=O)=O RSIJVJUOQBWMIM-UHFFFAOYSA-L 0.000 claims description 5
- 239000002893 slag Substances 0.000 claims description 3
- 239000002028 Biomass Substances 0.000 claims description 2
- 230000000996 additive effect Effects 0.000 claims description 2
- 238000000227 grinding Methods 0.000 claims description 2
- 238000010309 melting process Methods 0.000 claims 1
- 238000002156 mixing Methods 0.000 claims 1
- 239000004575 stone Substances 0.000 claims 1
- 230000007613 environmental effect Effects 0.000 abstract description 7
- 238000004140 cleaning Methods 0.000 abstract description 5
- 238000005260 corrosion Methods 0.000 abstract description 3
- 230000007797 corrosion Effects 0.000 abstract description 3
- 239000012467 final product Substances 0.000 abstract description 2
- 239000000155 melt Substances 0.000 abstract 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 10
- 229910000629 Rh alloy Inorganic materials 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 5
- 239000006063 cullet Substances 0.000 description 5
- 239000011491 glass wool Substances 0.000 description 5
- 230000014759 maintenance of location Effects 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- PXXKQOPKNFECSZ-UHFFFAOYSA-N platinum rhodium Chemical compound [Rh].[Pt] PXXKQOPKNFECSZ-UHFFFAOYSA-N 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 238000002791 soaking Methods 0.000 description 5
- 238000003860 storage Methods 0.000 description 4
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 3
- 239000003063 flame retardant Substances 0.000 description 3
- 229920001410 Microfiber Polymers 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 239000004568 cement Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000004567 concrete Substances 0.000 description 2
- 239000004088 foaming agent Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003658 microfiber Substances 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- CETPSERCERDGAM-UHFFFAOYSA-N ceric oxide Chemical compound O=[Ce]=O CETPSERCERDGAM-UHFFFAOYSA-N 0.000 description 1
- 229910000422 cerium(IV) oxide Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000011494 foam glass Substances 0.000 description 1
- 239000011464 hollow brick Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 238000004626 scanning electron microscopy Methods 0.000 description 1
Classifications
-
- 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
- C03C13/00—Fibre or filament compositions
- C03C13/06—Mineral fibres, e.g. slag wool, mineral wool, rock wool
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B37/00—Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
- C03B37/01—Manufacture of glass fibres or filaments
- C03B37/02—Manufacture of glass fibres or filaments by drawing or extruding, e.g. direct drawing of molten glass from nozzles; Cooling fins therefor
- C03B37/022—Manufacture of glass fibres or filaments by drawing or extruding, e.g. direct drawing of molten glass from nozzles; Cooling fins therefor from molten glass in which the resultant product consists of different sorts of glass or is characterised by shape, e.g. hollow fibres, undulated fibres, fibres presenting a rough surface
-
- 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
- C03C1/002—Use of waste materials, e.g. slags
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Geochemistry & Mineralogy (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Glass Compositions (AREA)
Abstract
本发明涉及一种以粉煤灰为主要原料的玻璃纤维及其制备方法,本发明的以粉煤灰为主要原料的玻璃纤维,包括以下质量百分比的原料组分:粉煤灰25‑75%、石英砂5‑30%、方解石5‑25%、白云石0~5%、其他成分5‑20%。本发明将所述质量配比的原料组分混合、研磨后加入添加剂得到混合料,进行熔制得到玻璃液,水淬后得到粉煤灰玻璃,经清洗、挑选、去污后,进行拉丝、烘干得到终产物玻璃纤维。本发明制备得到的玻璃纤维强度高、抗腐蚀、耐高温,且实现整个产业链的节能环保,具有非常大的经济效益、环境效益和社会效益,同时也具有非常好的发展前景。
The invention relates to a glass fiber with fly ash as the main raw material and a preparation method thereof. The glass fiber with fly ash as the main raw material of the present invention includes the following raw material components in mass percentage: fly ash 25-75% , quartz sand 5-30%, calcite 5-25%, dolomite 0-5%, other ingredients 5-20%. The present invention mixes and grinds the raw material components in the mass ratio, adds additives to obtain a mixture, melts it to obtain glass liquid, and obtains fly ash glass after water quenching. After cleaning, selecting and decontaminating, wire drawing, Dry to obtain the final product glass fiber. The glass fiber prepared by the invention has high strength, corrosion resistance and high temperature resistance, realizes energy saving and environmental protection of the whole industrial chain, has very large economic benefits, environmental benefits and social benefits, and also has very good development prospects.
Description
技术领域technical field
本发明属于玻璃纤维材料技术领域,特别涉及一种以粉煤灰为主要原料的玻璃纤维及其制备方法。The invention belongs to the technical field of glass fiber materials, in particular to a glass fiber with fly ash as the main raw material and a preparation method thereof.
背景技术Background technique
粉煤灰是煤粉燃烧后由烟气自锅炉中带出的粉状残留物。近年来,我国工业迅速发展,燃煤发电机组规模增大,同时存在燃煤品位低、单位发电量煤耗高等问题,粉煤灰排放量随之逐年增加,给我国生态环境建设及国民经济发展带来了严重的不利影响。目前对粉煤灰综合治理的途径已从过去的路基、填方、混凝土掺和料等方面的应用拓展到环保材料、泡沫玻璃、水泥原料、大体积混凝土制品等高级化利用。Fly ash is the powdery residue that is carried out from the boiler by the flue gas after the combustion of pulverized coal. In recent years, my country's industry has developed rapidly, and the scale of coal-fired power generation units has increased. At the same time, there are problems such as low coal grade and high coal consumption per unit of power generation. There were serious adverse effects. At present, the comprehensive management of fly ash has expanded from the past application of roadbed, filling, concrete admixture, etc. to advanced utilization of environmental protection materials, foam glass, cement raw materials, and large-volume concrete products.
赵同习等人于2010年12月申请了粉煤灰干混砂浆(申请号:201010608676.0)。蒋国平(宜兴市宏伟科技有限公司)于2012年10月申请了粉煤灰复合助磨剂发明专利(申请号:201210420974.6)。许庆华等人2013年5月申请了粉煤灰阻燃发泡剂发明专利(申请号:201310198238.5)。该发明公开了一种粉煤灰阻燃发泡剂,适用于生产阻燃灭火、轻质板材、轻质墙体和消音降噪产品。同年10月他们还申请了粉煤灰环保吸音板发明专利(申请号:201310475274.1)。刘林2014年10月申请了一种粉煤灰空心砖发明专利(申请号:201410551770.5)。胡成朔等人于2016年8月申请了一种粉煤灰水泥发明专利。Zhao Tongxi and others applied for fly ash dry-mixed mortar in December 2010 (application number: 201010608676.0). Jiang Guoping (Yixing Hongwei Technology Co., Ltd.) applied for the invention patent of fly ash composite grinding aid in October 2012 (application number: 201210420974.6). Xu Qinghua and others applied for the invention patent of fly ash flame retardant foaming agent in May 2013 (application number: 201310198238.5). The invention discloses a fly ash flame retardant foaming agent, which is suitable for producing flame retardant and fire extinguishing products, light boards, light walls and noise reduction products. In October of the same year, they also applied for a patent for the invention of fly ash environmental sound-absorbing panels (application number: 201310475274.1). Liu Lin applied for a patent for the invention of a fly ash hollow brick in October 2014 (application number: 201410551770.5). Hu Chengshuo and others applied for a patent for a fly ash cement invention in August 2016.
目前关于玻璃棉及玻璃纤维的专利也有部分。张振英于2013年6月申请了微纤维玻璃棉窑炉控制及生产工艺(申请号:201310467061.4)。栾晓于2013年10月申请了微纤维玻璃棉生产工艺(申请号:201310467061.4)。这些都是从玻璃棉及玻璃纤维的工艺等方面进行改进,但是不涉及粉煤灰。At present, there are also some patents on glass wool and glass fiber. Zhang Zhenying applied for the microfiber glass wool kiln control and production process in June 2013 (application number: 201310467061.4). Luan Xiao applied for the production process of microfiber glass wool in October 2013 (application number: 201310467061.4). These are improvements from glass wool and glass fiber technology, but do not involve fly ash.
发明内容Contents of the invention
本发明所要解决的技术问题是提供一种以粉煤灰为主要原料的玻璃纤维及其制备方法,本发明利用发电厂粉煤灰中含有较高的耐酸性氧化铝及氧化钙,结合石英砂等原料,制备玻璃纤维,实现整个产业链的节能环保,具有非常好的发展前景。The technical problem to be solved by the present invention is to provide a kind of glass fiber with fly ash as the main raw material and its preparation method. and other raw materials to prepare glass fibers and realize the energy saving and environmental protection of the entire industrial chain, which has very good development prospects.
本发明的一种以粉煤灰为主要原料的玻璃纤维,包括以下质量百分比的原料组分:粉煤灰25~75%、石英砂5~30%、方解石5~25%、白云石0~5%、其他成分5~20%。其中粉煤灰的组分含量优选45~75%。A glass fiber with fly ash as the main raw material of the present invention comprises the following raw material components in mass percentage: 25-75% of fly ash, 5-30% of quartz sand, 5-25% of calcite, 0-25% of dolomite 5%, other ingredients 5-20%. Wherein the component content of fly ash is preferably 45-75%.
所述粉煤灰为发电厂用粉煤灰,其中发电厂选自粉煤发电厂、煤泥发电厂或生物质发电厂中的一种或几种。The fly ash is fly ash for a power plant, wherein the power plant is selected from one or more of a pulverized coal power plant, a coal slime power plant or a biomass power plant.
所述其他成分为碎玻璃或工业矿渣。The other ingredients are cullet or industrial slag.
所述玻璃纤维的拉制直径为10~20μm。The drawing diameter of the glass fiber is 10-20 μm.
本发明所述的以粉煤灰为主要原料的玻璃纤维的制备方法,包括:The preparation method of the glass fiber taking fly ash as the main raw material of the present invention comprises:
(1)将粉煤灰、石英砂、方解石、白云石和其他成分均匀混合并研磨,后加入添加剂,得到混合料,其中其他成分为碎玻璃或工业矿渣;(1) Evenly mix and grind fly ash, quartz sand, calcite, dolomite and other components, and then add additives to obtain a mixture, wherein other components are broken glass or industrial slag;
(2)将步骤(1)得到的混合料进行熔制,得到玻璃液,水淬后得到粉煤灰玻璃;(2) melting the mixture obtained in step (1) to obtain molten glass, and obtaining fly ash glass after water quenching;
(3)将步骤(2)得到的粉煤灰玻璃经清洗、挑选、去污后放入铂铑合金坩埚内,进行拉丝,然后烘干得到终产物玻璃纤维。(3) Put the fly ash glass obtained in the step (2) into a platinum-rhodium alloy crucible after being cleaned, selected and decontaminated, draw wire, and then dry to obtain the final product glass fiber.
所述步骤(1)中的添加剂为玻璃澄清剂,为芒硝或CeO2,但不限于这两种玻璃澄清剂。其中芒硝的用量为混合料总量的0.1~0.3%,CeO2的用量为混合料总量的0.1~0.4%。The additive in the step (1) is a glass clarifier, which is Glauber's salt or CeO 2 , but not limited to these two glass clarifiers. Wherein the consumption of Glauber's salt is 0.1-0.3% of the total amount of the mixture, and the consumption of CeO2 is 0.1-0.4 % of the total amount of the mixture.
所述步骤(2)中的熔制的工艺参数为:熔制温度1350~1450℃,熔制时间为3~4h。The technological parameters of the melting in the step (2) are: the melting temperature is 1350-1450° C., and the melting time is 3-4 hours.
所述步骤(3)中的拉丝的工艺参数为:先升温至1300~1400℃,保温1.5~2.5h,根据玻璃液粘度,在1200~1280℃进行拉丝。The technical parameters of the wire drawing in the step (3) are as follows: first, the temperature is raised to 1300-1400° C., kept for 1.5-2.5 hours, and the wire drawing is carried out at 1200-1280° C. according to the viscosity of the glass liquid.
所述步骤(3)中的烘干的工艺参数为:烘干温度为85~110℃,烘干时间为6~12h。The technical parameters of the drying in the step (3) are as follows: the drying temperature is 85-110° C., and the drying time is 6-12 hours.
所述步骤(3)中的拉丝过程中涂敷浸润剂。The sizing agent is applied during the drawing process in the step (3).
有益效果Beneficial effect
(1)本发明的以粉煤灰为主要原料的玻璃纤维,与常规的玻璃棉及玻璃纤维进行各项性能对比,结果发现其具有强度高、抗腐蚀、耐高温等性能。(1) The glass fiber with fly ash as the main raw material of the present invention is compared with conventional glass wool and glass fiber in various properties, and it is found that it has high strength, corrosion resistance, high temperature resistance and other properties.
(2)本发明的以粉煤灰为主要原料的玻璃纤维,利用粉煤灰中含有较高的耐酸性氧化铝及氧化钙,结合石英砂等原料,实现整个产业链的节能环保,具有非常大的经济效益、环境效益和社会效益,同时也具有非常好的发展前景。(2) The glass fiber with fly ash as the main raw material of the present invention utilizes the high acid-resistant alumina and calcium oxide contained in the fly ash, combined with raw materials such as quartz sand, to realize energy saving and environmental protection of the entire industrial chain, and has a very Great economic benefits, environmental benefits and social benefits, but also has a very good development prospects.
附图说明Description of drawings
图1是实施例2制备的45%粉煤灰玻璃纤维的SEM图。Fig. 1 is the SEM image of the 45% fly ash glass fiber prepared in Example 2.
图2是实施例1~4制备的不同粉煤灰含量的玻璃纤维的拉伸强度曲线图。Fig. 2 is a graph showing the tensile strength of glass fibers with different fly ash contents prepared in Examples 1-4.
图3是实施例1~2制备的不同粉煤灰含量的玻璃纤维的XRD图。Fig. 3 is an XRD pattern of glass fibers with different fly ash contents prepared in Examples 1-2.
具体实施方式detailed description
下面结合具体实施例,进一步阐述本发明。应理解,这些实施例仅用于说明本发明而不用于限制本发明的范围。此外应理解,在阅读了本发明讲授的内容之后,本领域技术人员可以对本发明作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。Below in conjunction with specific embodiment, further illustrate the present invention. It should be understood that these examples are only used to illustrate the present invention and are not intended to limit the scope of the present invention. In addition, it should be understood that after reading the teachings of the present invention, those skilled in the art can make various changes or modifications to the present invention, and these equivalent forms also fall within the scope defined by the appended claims of the present application.
实施例1Example 1
某火力发电厂粉煤灰组分的质量分数如表1所示。The mass fraction of fly ash components in a thermal power plant is shown in Table 1.
表1粉煤灰组分表Table 1 Fly ash composition list
(1)称取如下质量百分比的原料组分:粉煤灰25%、石英砂45%、方解石10%、白云石5%、碎玻璃15%,配制成配合料,进行研磨、混匀,加入用量为混合料的0.1%的CeO2玻璃澄清剂,得到混合料;(1) Weigh the following raw material components in mass percentage: 25% of fly ash, 45% of quartz sand, 10% of calcite, 5% of dolomite, 15% of cullet, and prepare batch materials, grind and mix, add Consumption is the 0.1% CeO of mixture 2 Glass clarifying agent, obtain mixture;
(2)将混合料加到坩埚中,并置于熔化炉中;在1400℃温度下,熔制3h,得到无缺陷的玻璃液,水淬后得到粉煤灰玻璃;(2) Add the mixture into the crucible and place it in a melting furnace; melt it at 1400°C for 3 hours to obtain a defect-free molten glass, and obtain fly ash glass after water quenching;
(3)将上述粉煤灰玻璃经清洗、挑选、去污后,加入到铂铑合金坩埚内,升温到1350℃后保温2小时后,然后根据玻璃液粘度在1200℃进行拉丝,并在拉丝过程中涂覆浸润剂,拉好的玻璃纤维在85℃下烘干12小时,得到玻璃纤维,编号包装后保存。(3) After cleaning, selecting and decontaminating the above-mentioned fly ash glass, add it into a platinum-rhodium alloy crucible, heat it up to 1350°C and keep it warm for 2 hours, then draw it at 1200°C according to the viscosity of the glass liquid, and then draw During the process, the sizing agent is coated, and the drawn glass fibers are dried at 85°C for 12 hours to obtain glass fibers, which are numbered and packaged for storage.
测试本实施例得到的玻璃纤维的拉伸强度性能,结果如图2所示,拉伸强度达到3.16GPa。测试本实施例得到的玻璃纤维的软化点温度高达890℃,3mol/L盐酸浸润24小时后质量保持率达到91.3%。使用X射线衍射仪(XRD)表征本实施例得到的玻璃纤维的结构,结果表明为非晶的玻璃态结构,如图3所示。The tensile strength performance of the glass fiber obtained in this embodiment was tested, and the result is shown in FIG. 2 , the tensile strength reached 3.16GPa. The softening point temperature of the glass fiber obtained in this example is as high as 890° C., and the mass retention rate reaches 91.3% after soaking with 3 mol/L hydrochloric acid for 24 hours. The structure of the glass fiber obtained in this embodiment was characterized by X-ray diffractometer (XRD), and the result showed that it was an amorphous glass structure, as shown in FIG. 3 .
实施例2Example 2
采用实施例1中相同的某火力发电厂粉煤灰。Adopt the same certain thermal power plant fly ash among the embodiment 1.
(1)称取如下质量百分比的原料组分:粉煤灰45%、石英砂30%、方解石12%、白云石3%、碎玻璃10%,配制成配合料,进行研磨、混匀,加入用量为混合料的0.2%的CeO2玻璃澄清剂,得到混合料;(1) Weigh the raw material components in the following mass percentages: 45% fly ash, 30% quartz sand, 12% calcite, 3% dolomite, 10% cullet, and make batches, grind, mix, add Consumption is the 0.2% CeO of mixture 2 glass clarifying agent, obtains mixture;
(2)将混合料加到坩埚中,并置于熔化炉中;在1420℃温度下,熔制4h,得到无缺陷的玻璃液,水淬后得到粉煤灰玻璃;(2) Add the mixture to the crucible and place it in a melting furnace; melt it at 1420°C for 4 hours to obtain a defect-free molten glass, and obtain fly ash glass after water quenching;
(3)将上述粉煤灰玻璃经清洗、挑选、去污后,加入到铂铑合金坩埚内,升温到1350℃后保温2小时后,然后根据玻璃液粘度在1240℃进行拉丝,并在拉丝过程中涂覆浸润剂,拉好的玻璃纤维在100℃下烘干9小时,得到玻璃纤维,编号包装后保存。(3) After cleaning, selecting and decontaminating the above-mentioned fly ash glass, put it into a platinum-rhodium alloy crucible, heat it up to 1350°C and keep it warm for 2 hours, then draw it at 1240°C according to the viscosity of the glass liquid, and then draw it in the drawing During the process, the sizing agent is coated, and the drawn glass fibers are dried at 100°C for 9 hours to obtain glass fibers, which are numbered and packaged for storage.
使用扫描电子显微镜(SEM)表征本实施例得到的玻璃纤维的形貌,结果如图1所示。测试本实施例得到的玻璃纤维的拉伸强度性能,结果如图2所示,拉伸强度达到3.25GPa。测试本实施例得到的玻璃纤维的软化点温度高达910℃,3mol/L盐酸浸润24小时后质量保持率达到97.5%。使用X射线衍射仪(XRD)表征本实施例得到的玻璃纤维的结构,结果表明为非晶的玻璃态结构,如图3所示。The morphology of the glass fiber obtained in this example was characterized by scanning electron microscopy (SEM), and the results are shown in FIG. 1 . The tensile strength performance of the glass fiber obtained in this embodiment was tested, and the result is shown in FIG. 2 , the tensile strength reached 3.25 GPa. The softening point temperature of the glass fiber obtained in this example is as high as 910° C., and the mass retention rate reaches 97.5% after soaking with 3 mol/L hydrochloric acid for 24 hours. The structure of the glass fiber obtained in this embodiment was characterized by X-ray diffractometer (XRD), and the result showed that it was an amorphous glass structure, as shown in FIG. 3 .
实施例3Example 3
采用实施例1中相同的某火力发电厂粉煤灰。Adopt the same certain thermal power plant fly ash among the embodiment 1.
(1)称取如下质量百分比的原料组分:粉煤灰55%、石英砂20%、方解石10%、白云石3%、碎玻璃12%,配制成配合料,进行研磨、混匀,加入用量为混合料的0.2%的芒硝玻璃澄清剂,得到混合料;(1) Weigh the following raw material components in mass percentage: 55% of fly ash, 20% of quartz sand, 10% of calcite, 3% of dolomite, 12% of cullet, and prepare batch materials, grind and mix, add Consumption is the Glauber's salt glass clarifying agent of 0.2% of the mixture to obtain the mixture;
(2)将混合料加到坩埚中,并置于熔化炉中;在1380℃温度下,熔制3h,得到无缺陷的玻璃液,水淬后得到粉煤灰玻璃;(2) Add the mixture into the crucible and place it in a melting furnace; melt it at 1380°C for 3 hours to obtain a defect-free molten glass, and obtain fly ash glass after water quenching;
(3)将上述粉煤灰玻璃经清洗、挑选、去污后,加入到铂铑合金坩埚内,升温到1350℃后保温2小时后,然后根据玻璃液粘度在1260℃进行拉丝,并在拉丝过程中涂覆浸润剂,拉好的玻璃纤维在85℃下烘干12小时,得到玻璃纤维,编号包装后保存。(3) After cleaning, selecting and decontaminating the above-mentioned fly ash glass, add it into a platinum-rhodium alloy crucible, heat it up to 1350°C and keep it warm for 2 hours, then draw it at 1260°C according to the viscosity of the glass liquid, and then draw During the process, the sizing agent is coated, and the drawn glass fibers are dried at 85°C for 12 hours to obtain glass fibers, which are numbered and packaged for storage.
测试本实施例得到的玻璃纤维的拉伸强度性能,如图2所示所示,拉伸强度达到3.36GPa。测试本实施例得到的玻璃纤维的软化点温度高达925℃,3mol/L盐酸浸润24小时后质量保持率达到98.2%。The tensile strength performance of the glass fiber obtained in this embodiment was tested, and as shown in FIG. 2 , the tensile strength reached 3.36GPa. The softening point temperature of the glass fiber obtained in this example is as high as 925° C., and the mass retention rate reaches 98.2% after soaking with 3 mol/L hydrochloric acid for 24 hours.
实施例4Example 4
采用实施例1中相同的某火力发电厂粉煤灰。Adopt the same certain thermal power plant fly ash among the embodiment 1.
(1)称取如下质量百分比的原料组分:粉煤灰75%、石英砂5%、方解石10%、白云石3%、碎玻璃7%,配制成配合料,进行研磨、混匀,加入用量为混合料的0.3%的芒硝玻璃澄清剂,得到混合料;(1) Weigh the following raw material components in mass percentage: 75% of fly ash, 5% of quartz sand, 10% of calcite, 3% of dolomite, 7% of cullet, and prepare batch materials, grind and mix, add Consumption is the Glauber's salt glass clarifying agent of 0.3% of the mixture to obtain the mixture;
(2)将混合料加到坩埚中,并置于熔化炉中;在1400℃温度下,熔制3h,得到无缺陷的玻璃液,水淬后得到粉煤灰玻璃;(2) Add the mixture into the crucible and place it in a melting furnace; melt it at 1400°C for 3 hours to obtain a defect-free molten glass, and obtain fly ash glass after water quenching;
(3)将上述粉煤灰玻璃经清洗、挑选、去污后,加入到铂铑合金坩埚内,升温到1350℃后保温2小时后,然后根据玻璃液粘度在1280℃进行拉丝,并在拉丝过程中涂覆浸润剂,拉好的玻璃纤维在110℃下烘干6小时,得到玻璃纤维,编号包装后保存。(3) After cleaning, selecting and decontaminating the above-mentioned fly ash glass, put it into a platinum-rhodium alloy crucible, heat it up to 1350°C and keep it warm for 2 hours, then draw it at 1280°C according to the viscosity of the glass liquid, and draw it During the process, the sizing agent is applied, and the drawn glass fibers are dried at 110°C for 6 hours to obtain glass fibers, which are numbered and packaged for storage.
测试本实施例得到的玻璃纤维的拉伸强度性能,结果如图2所示,拉伸强度达到3.18GPa。测试本实施例得到的玻璃纤维的软化点温度高达905℃,3mol/L盐酸浸润24小时后质量保持率达到94.6%。The tensile strength performance of the glass fiber obtained in this embodiment was tested, and the result is shown in FIG. 2 , the tensile strength reached 3.18 GPa. The softening point temperature of the glass fiber obtained in this example is as high as 905° C., and the mass retention rate reaches 94.6% after soaking with 3 mol/L hydrochloric acid for 24 hours.
对比例1Comparative example 1
利用石英砂、氧化铝等工业原料,采用高温熔融法制备得到普通E玻璃纤维。Ordinary E-glass fiber is prepared by high-temperature melting method by using industrial raw materials such as quartz sand and alumina.
测试本对比例得到的玻璃纤维的拉伸强度性能,拉伸强度为3.08GPa,软化点温度为850℃,3mol/L盐酸浸润24小时后质量保持率仅为76.5%。与实施例1-4以粉煤灰为主要原料制备得到的玻璃纤维的性能对比如表2所示。The tensile strength performance of the glass fiber obtained in this comparative example was tested. The tensile strength was 3.08GPa, the softening point temperature was 850°C, and the mass retention rate was only 76.5% after soaking in 3mol/L hydrochloric acid for 24 hours. Table 2 shows the performance comparison with the glass fiber prepared by using fly ash as the main raw material in Examples 1-4.
表2不同组分玻璃纤维产品性能对比Table 2 Performance comparison of glass fiber products with different components
可见本发明的以粉煤灰为主要原料的玻璃纤维与普通玻璃纤维产品性能对比结果表明:本发明的以粉煤灰为主要原料的玻璃纤维具有强度高、抗腐蚀且耐高温的优异性能。It can be seen that the performance comparison between the glass fiber with fly ash as the main raw material of the present invention and ordinary glass fiber products shows that the glass fiber with fly ash as the main raw material of the present invention has excellent properties of high strength, corrosion resistance and high temperature resistance.
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CN110590170A (en) * | 2019-09-30 | 2019-12-20 | 九和同创碳金(宁夏)新材料科技有限公司 | Fly ash-based inorganic fiber and preparation method thereof |
CN111285639A (en) * | 2020-03-16 | 2020-06-16 | 董卫兵 | Special antifreezing and anti-erosion concrete for salinized areas and preparation method thereof |
CN117466538A (en) * | 2023-12-27 | 2024-01-30 | 东华大学 | Medium-alkali glass fiber with waste diatomite as main raw material and preparation method thereof |
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CN104310788A (en) * | 2014-09-26 | 2015-01-28 | 东华大学 | Glass fiber taking blast furnace slag as raw material and preparation method of glass fiber |
CN104496189A (en) * | 2014-12-31 | 2015-04-08 | 济南大学 | Boron-free high-performance glass fiber taking pulverized fuel ash and desalted river sand as raw materials, as well as preparation method thereof |
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CN104310788A (en) * | 2014-09-26 | 2015-01-28 | 东华大学 | Glass fiber taking blast furnace slag as raw material and preparation method of glass fiber |
CN104496189A (en) * | 2014-12-31 | 2015-04-08 | 济南大学 | Boron-free high-performance glass fiber taking pulverized fuel ash and desalted river sand as raw materials, as well as preparation method thereof |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
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CN110590170A (en) * | 2019-09-30 | 2019-12-20 | 九和同创碳金(宁夏)新材料科技有限公司 | Fly ash-based inorganic fiber and preparation method thereof |
CN111285639A (en) * | 2020-03-16 | 2020-06-16 | 董卫兵 | Special antifreezing and anti-erosion concrete for salinized areas and preparation method thereof |
CN113185162A (en) * | 2020-03-16 | 2021-07-30 | 董卫兵 | Special antifreezing and anti-erosion concrete for salinized areas |
CN113185162B (en) * | 2020-03-16 | 2023-08-04 | 宁波中海建材有限公司 | Special anti-freezing and anti-erosion concrete for salinized areas |
CN117466538A (en) * | 2023-12-27 | 2024-01-30 | 东华大学 | Medium-alkali glass fiber with waste diatomite as main raw material and preparation method thereof |
CN117466538B (en) * | 2023-12-27 | 2024-03-01 | 东华大学 | A medium-alkali glass fiber using waste diatomite as the main raw material and its preparation method |
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