CN113788623B - Method for preparing foam glass ceramics by secondary aluminum ash without pretreatment - Google Patents
Method for preparing foam glass ceramics by secondary aluminum ash without pretreatment Download PDFInfo
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- CN113788623B CN113788623B CN202111124425.XA CN202111124425A CN113788623B CN 113788623 B CN113788623 B CN 113788623B CN 202111124425 A CN202111124425 A CN 202111124425A CN 113788623 B CN113788623 B CN 113788623B
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- 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
- C03C11/00—Multi-cellular glass ; Porous or hollow glass or glass particles
- C03C11/007—Foam glass, e.g. obtained by incorporating a blowing agent and heating
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/06—Other methods of shaping glass by sintering, e.g. by cold isostatic pressing of powders and subsequent sintering, by hot pressing of powders, by sintering slurries or dispersions not undergoing a liquid phase reaction
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/08—Other methods of shaping glass by foaming
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B32/00—Thermal after-treatment of glass products not provided for in groups C03B19/00, C03B25/00 - C03B31/00 or C03B37/00, e.g. crystallisation, eliminating gas inclusions or other impurities; Hot-pressing vitrified, non-porous, shaped glass products
- C03B32/02—Thermal crystallisation, e.g. for crystallising glass bodies into glass-ceramic articles
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- 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
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- 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
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- 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
- C03C10/00—Devitrified glass ceramics, i.e. glass ceramics having a crystalline phase dispersed in a glassy phase and constituting at least 50% by weight of the total composition
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
Abstract
The invention discloses a method for preparing foam glass ceramics by secondary aluminum ash without pretreatment, belonging to the field of solid waste comprehensive utilization. And (3) performing ball milling on the secondary aluminum ash, the waste glass, the viscosity regulator and the foam stabilizer, molding, and performing synchronous foaming and crystallization to obtain the foam glass ceramics. Alumina in the waste glass and the secondary aluminum ash provides a silicon source and an aluminum source of a glass network for the foam glass ceramics, and the viscosity regulator provides a calcium source. The foam stabilizer can change the performance of the foam microcrystalline glass melt and stabilize the structure of bubbles. The method utilizes the alumina in the secondary aluminum ash slag to provide a glass network body for the foam glass ceramics without nitrogen removal and desalting pretreatment, takes the aluminum nitride in the secondary aluminum ash slag as a foaming agent, converts potassium salt and sodium salt in the foaming agent into a glass phase, and takes fluoride as a fluxing agent, thereby not only saving energy, reducing consumption, having high economic benefit and reducing environmental pollution, but also realizing harmless disposal and high-value utilization of the secondary aluminum ash slag, and having the advantages of short flow and easy industrialization.
Description
Technical Field
The invention belongs to the field of comprehensive utilization of solid wastes, and particularly relates to a method for preparing foam microcrystalline glass from secondary aluminum ash without pretreatment.
Background
The aluminous ash is dangerous solid waste formed by the reaction of molten aluminum and air in the aluminum smelting process, and the conservative estimated annual discharge amount is 30More than 0 million tons. The aluminous ash slag is divided into primary aluminous ash slag and secondary aluminous ash slag, the primary aluminous ash slag contains 30-70% of aluminium, and metal aluminium is generally recovered through secondary smelting, and slag generated in the process is called secondary aluminous ash slag. The secondary aluminum ash contains water-soluble chloride (such as NaCl and KCl), trace heavy metals and toxic ions (F) - ，CN - ) When the secondary aluminum ash slag is easy to enter into the ecological environment, toxic and flammable gas can be generated when the secondary aluminum ash slag is exposed in the external environment, and the serious influence is caused on the health and the environment of people, so the harmless treatment of the secondary aluminum ash slag needs to be solved urgently.
At present, harmless treatment and resource utilization in secondary aluminum ash slag mainly focus on using hydrometallurgy and a heat treatment method. Such as water washing, acid leaching and alkaline leaching, and realizes the recovery of valuable elements in the aluminous ash. The water washing is usually used as a pretreatment process for improving the recovery rate of aluminum, so that salt in the aluminum ash can be recovered, aluminum nitride can be hydrolyzed, and the influence of impurities on the leaching process is reduced. The alkaline leaching and acid leaching mainly promote aluminum to enter leaching solution in the form of ions, and valuable products such as activated alumina and eta-Al are obtained by the processes of coprecipitation, purification, roasting and the like 2 O 3 And the like, thereby achieving the purpose of recovering aluminum. The use of secondary aluminum ash for making cement fillers, geopolymers and concrete blocks has also been studied. However, chlorine salt existing in the secondary aluminous ash has an interference effect on the hydration reaction of cement, so that the mechanical property of the building material is reduced; aluminum nitride also decomposes ammonia over time. Although water washing pretreatment can be used for removing chloride salt, aluminum nitride can still exist in the building material due to incomplete hydrolysis, thereby releasing ammonia gas, and the requirement of safe disposal is not met.
Chinese patent No. CN 112794353A discloses a method and a device for preparing polyaluminum chloride by recycling aluminum ash, which are used for obtaining the polyaluminum chloride by hydrolysis, drying, acid dissolution, alkali dissolution and filtration centrifugation, but have high water consumption and generate a large amount of waste alkali and waste acid.
The Chinese invention patent (CN 112553470A) discloses a method for recovering aluminum hydroxide powder by using titanium white waste acid and secondary aluminum ash, which removes nitrogen and salt by water leaching, and uses the titanium white waste acid and part of concentrated sulfuric acid as leaching solution to carry out acid leaching on the secondary aluminum ash slag, but the acid consumption is large and the process is complex.
Chinese invention patent (CN 108275708B) discloses a secondary aluminum ash resource utilization method, which comprises the steps of grinding secondary aluminum ash into powder, then flushing the powder with steam under a high pressure condition, recovering nitrogen and hydrogen fluoride, carrying out suction filtration, evaporation and crystallization on high-concentration aluminum mortar, recovering chlorine salt, roasting a filtered solid phase at 1300-1500 ℃ to recover fluoride, adding an alkali flux to carry out impurity removal smelting at 800-1100 ℃, then adding liquid to carry out solid-liquid separation, and finally calcining a leachate at more than 1000 ℃ to obtain aluminum oxide.
The Chinese invention patent (CN 108383142B) discloses a method for producing alumina by recycling regenerated aluminum ash, which obtains alumina by grinding, cleaning, low-temperature alkaline smelting, water leaching, impurity removal of leachate, precipitation of aluminum hydroxide and high-temperature roasting, but can generate a large amount of wastewater containing F, cl and ammonia nitrogen.
Chinese invention patent (CN 106478020A) discloses a method for preparing a baking-free brick from waste aluminum ash, which is to crush, mix, mold and maintain the waste aluminum ash and raw materials such as water-quenched slag, silica fume powder, anhydrous calcium sulfate and the like to obtain the baking-free brick, but the problem that aluminum nitride in the aluminum ash is hydrolyzed under the condition of water existence to generate ammonia gas is not solved.
Chinese patent of invention (CN 11056336A) discloses a method for preparing glass ceramics by aluminum ash without desalting and denitriding, which mixes secondary aluminum ash generated after aluminum is extracted from calcium aluminate with calcium lime, waste glass and the like to prepare glass ceramics, and obtains the glass ceramics by nucleation-crystallization heat treatment after the aluminum ash is converted into glass at 1200-1500 ℃, but the method needs two heat treatments and the temperature can reach as high as 1500 ℃, the energy consumption is high, the heat treatment process is complex, and the gas generated by aluminum nitride in the aluminum ash is not effectively utilized.
Disclosure of Invention
The invention aims to fully utilize the intrinsic characteristics of secondary aluminum ash, and provide a method for preparing foam glass ceramics by the secondary aluminum ash without pretreatment.
The invention is realized by the following technical scheme:
a method for preparing foam glass ceramics by secondary aluminum ash without pretreatment comprises the steps of ball-milling the secondary aluminum ash, waste glass, a viscosity regulator and a foam stabilizer, molding, synchronously foaming and crystallizing to obtain the foam glass ceramics; the waste glass and alumina in the secondary aluminum ash slag are used as a silicon source and an aluminum source of a glass network for the foam glass ceramics, the secondary aluminum ash slag is used as a foaming agent, a nucleating agent and a fluxing agent for preparing the foam glass ceramics, the viscosity regulator is used as a calcium source for the foam glass ceramics, and the foam stabilizer can change the melt performance of the foam glass ceramics and stabilize the bubble structure.
Furthermore, the raw material ratio is 25-40 wt.% of secondary aluminum ash, 30-40 wt.% of waste glass, 15-30 wt.% of viscosity regulator and 5-10 wt.% of foam stabilizer.
Further, the viscosity regulator is one or more of quicklime, calcium carbonate and borax; the foam stabilizer is trisodium phosphate (Na) 3 PO 4 )。
A method for preparing foam glass ceramics by secondary aluminum ash without pretreatment comprises the following specific steps:
s1, ball milling: ball-milling secondary aluminum ash, waste glass, a viscosity regulator and a foam stabilizer to obtain a uniform mixture;
s2, forming: pouring the mixture into a mould, and pressing and forming the mixture by using a press;
s3, synchronous foaming and crystallization: and carrying out heat treatment on the raw materials subjected to compression molding to obtain the foam microcrystalline glass.
Further, the ball milling process parameter is that the ball milling rotation speed is 100-500 rpm, the ball milling is carried out for 1-4h, and the mixture is sieved by a 100-mesh sieve.
Furthermore, the molding parameter is pressure of 20-30 MPa, and is maintained for 20-60 s.
Further, the synchronous foaming crystallization heat treatment system is that the temperature is kept for 20-60 min at 1000-1350 ℃.
The principle of the invention is as follows:
(1) The mechanical ball milling process causes the temperature and the pressure of an impact friction point to rise, causes the crystal defect diffusion and the atom local rearrangement of the mixture, reduces the bonding energy of oxygen, nitrogen, silicon and aluminum, improves the specific surface area of raw material particles, promotes foaming components in secondary aluminum ash slag to easily generate chemical reactions such as oxidation, hydrolysis and the like, simultaneously promotes the particle size reduction of the mixture in the ball milling process, increases the stacking density of the particles, uniformly distributes the foaming components, the viscosity regulator, the foam stabilizer and the like, and is favorable for the uniform diffusion of gas after forming a melt.
(2) The waste glass is firstly used for forming a melt at high temperature, and simultaneously, potassium salt, sodium salt and fluoride in secondary aluminum ash are used for reducing the melting point of the materials, so that the secondary aluminum ash and a viscosity regulator form a melt zone to promote the foam stabilizer to form [ PO ] 4 ]Tetrahedrons complement the glass network structure and retain bubbles within the melt.
(3) The trace heavy metals in the secondary aluminum ash are used as nucleating agents of the glass body, so that the crystal phase in the raw materials is promoted to be separated out, and the mechanical property of the product is enhanced.
(4) The gas temperature (800-1100 ℃) generated by the foaming component is higher than the softening temperature (more than 500 ℃) of the waste glass, thereby being beneficial to wrapping a gas phase by a melt and forming a solid-liquid-gas three-phase equilibrium state.
The invention has the beneficial technical effects that:
(1) According to the method, the secondary aluminum ash and the waste glass are used as a silica-aluminum source, the aluminum nitride existing in the secondary aluminum ash and the waste glass is used as a foaming component, so that the consumption of a foaming agent is reduced, and the problem of removing nitrogen from the secondary aluminum ash is solved;
(2) The method realizes green and efficient circulation of all components of the secondary aluminum ash;
(3) The method has the advantages of simple process, low cost, no pollution and wide applicability, and is easy for industrialization.
Drawings
FIG. 1 is a schematic flow chart of a method for preparing foam glass ceramics by using secondary aluminum ash without pretreatment in the embodiment of the invention.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more clearly understood, the present invention is further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
On the contrary, the invention is intended to cover alternatives, modifications, equivalents and alternatives which may be included within the spirit and scope of the invention as defined by the appended claims. Furthermore, in the following detailed description of the present invention, certain specific details are set forth in order to provide a thorough understanding of the present invention. It will be apparent to one skilled in the art that the present invention may be practiced without these specific details.
Example 1
Ball-milling 40wt.% secondary aluminous ash, 30wt.% waste glass, 20wt.% viscosity regulator and 10wt.% foam stabilizer in a mechanical ball mill for 2h, setting the ball-milling rotation speed at 400rpm, keeping the mixture at the pressure of 20MPa for 40s, and then keeping the temperature of the pressed sample at 1100 ℃ for 25min to obtain the foam microcrystalline glass with the porosity of 65% and the compressive strength of 8.23MPa.
Example 2
And (3) carrying out ball milling on 38wt.% secondary aluminous ash, 32wt.% waste glass, 25wt.% viscosity regulator and 5wt.% foam stabilizer in a mechanical ball mill for 3h, setting the ball milling rotation speed at 400rpm, keeping the mixture at the pressure of 22MPa for 30s, and then keeping the temperature of the pressed sample at 1150 ℃ for 30min to obtain the foamed microcrystalline glass with the porosity of 71% and the compressive strength of 7.40MPa.
Example 3
Ball-milling 34wt.% secondary aluminous ash, 35wt.% waste glass, 22wt.% viscosity regulator and 9wt.% foam stabilizer in a mechanical ball mill for 1h, setting the ball-milling speed at 500rpm, keeping the mixture at 23MPa for 32s, and then keeping the temperature of the pressed sample at 1180 ℃ for 35min to obtain the foam microcrystalline glass with the porosity of 74.2% and the compressive strength of 7.12MPa.
Example 4
And (3) ball-milling 33wt.% secondary aluminous ash, 39wt.% waste glass, 19wt.% viscosity regulator and 9wt.% foam stabilizer in a mechanical ball mill for 1.5h, setting the ball-milling rotation speed at 450rpm, keeping the mixture at the pressure of 24MPa for 37s, and then keeping the temperature of the pressed sample at 1050 ℃ for 40min to obtain the foamed microcrystalline glass with the porosity of 61.23% and the compressive strength of 14.33MPa.
Example 5
And (3) ball-milling 28wt.% secondary aluminous ash, 40wt.% waste glass, 24wt.% viscosity regulator and 8wt.% foam stabilizer in a mechanical ball mill for 2.5h, setting the ball-milling rotation speed at 480rpm, keeping the mixture at the pressure of 25MPa for 34s, and then keeping the temperature of the pressed sample at 1080 ℃ for 45min to obtain the foamed microcrystalline glass with the porosity of 62.35% and the compressive strength of 12.53MPa.
Example 6
And (3) ball-milling 39wt.% secondary aluminous ash, 38wt.% waste glass, 15wt.% viscosity regulator and 7wt.% foam stabilizer in a mechanical ball mill for 3.5h, setting the ball-milling rotation speed at 200rpm, keeping the mixture at the pressure of 30MPa for 20s, and then keeping the temperature of the pressed sample at 1120 ℃ for 28min to obtain the foamed microcrystalline glass with the porosity of 72.25% and the compressive strength of 14.14MPa.
Example 7
And (3) ball-milling 28wt.% secondary aluminous ash, 37wt.% waste glass, 29wt.% viscosity regulator and 6wt.% foam stabilizer in a mechanical ball mill for 4h, setting the ball-milling rotation speed at 100rpm, keeping the mixture at the pressure of 28MPa for 40s, and then keeping the temperature of the pressed sample at 1000 ℃ for 60min to obtain the foam microcrystalline glass with the porosity of 55.12% and the compressive strength of 15MPa.
Example 8
And (2) carrying out ball milling on 37wt.% secondary aluminous clinker, 36wt.% waste glass, 17wt.% viscosity regulator and 10wt.% foam stabilizer in a mechanical ball mill for 2 hours, setting the ball milling speed at 500rpm, keeping the mixture at the pressure of 21MPa for 42s, and then keeping the temperature of a pressed sample at 1080 ℃ for 55min to obtain the foam microcrystalline glass with the porosity of 58.02% and the compressive strength of 13.45MPa.
Example 9
And (3) ball-milling 36wt.% secondary aluminous clinker, 34wt.% waste glass, 20wt.% viscosity regulator and 10wt.% foam stabilizer in a mechanical ball mill for 3 hours, setting the ball-milling rotation speed at 480rpm, keeping the mixture at 29MPa for 55s, and then keeping the temperature of the pressed sample at 1040 ℃ for 57min to obtain the foamed microcrystalline glass with the porosity of 57.12% and the compressive strength of 11.20MPa.
Example 10
And (3) ball-milling 35wt.% secondary aluminous ash, 31wt.% waste glass, 26wt.% viscosity regulator and 8wt.% foam stabilizer in a mechanical ball mill for 2.8h, setting the ball-milling rotation speed at 250rpm, keeping the mixture at the pressure of 27MPa for 50s, and then keeping the temperature of the pressed sample at 1020 ℃ for 59min to obtain the foamed microcrystalline glass with the porosity of 60.12% and the compressive strength of 13.02MPa.
Example 11
And (3) ball-milling 25wt.% secondary aluminous clinker, 35wt.% waste glass, 30wt.% viscosity regulator and 10wt.% foam stabilizer in a mechanical ball mill for 1.8h, setting the ball-milling rotating speed at 200rpm, keeping the mixture at the pressure of 28MPa for 20s, and then keeping the temperature of the pressed sample at 1060 ℃ for 32min to obtain the foamed microcrystalline glass with the porosity of 65.21% and the compressive strength of 14.02MPa.
Example 12
And (3) carrying out ball milling on 26wt.% secondary aluminous clinker, 36wt.% waste glass, 28wt.% viscosity regulator and 10wt.% foam stabilizer in a mechanical ball mill for 4 hours, setting the ball milling speed at 300rpm, keeping the mixture at the pressure of 24MPa for 38s, and then keeping the temperature of the pressed sample at 1140 ℃ for 28min to obtain the foam microcrystalline glass with the porosity of 67.12% and the compressive strength of 9.45MPa.
Example 13
And (3) ball-milling 27wt.% secondary aluminous ash, 33wt.% waste glass, 30wt.% viscosity regulator and 10wt.% foam stabilizer in a mechanical ball mill for 4h, setting the ball-milling rotation speed at 380rpm, keeping the mixture at the pressure of 25MPa for 40s, and then keeping the temperature of the pressed sample at 1160 ℃ for 50min to obtain the foamed microcrystalline glass with the porosity of 50% and the compressive strength of 14.12MPa.
Example 14
And (3) ball-milling 29wt.% secondary aluminous ash, 34wt.% waste glass, 30wt.% viscosity regulator and 7wt.% foam stabilizer in a mechanical ball mill for 3h, setting the ball-milling rotation speed at 450rpm, keeping the mixture at the pressure of 22MPa for 23s, and then keeping the temperature of the pressed sample at 1200 ℃ for 25min to obtain the foamed microcrystalline glass with the porosity of 72.1% and the compressive strength of 7.25MPa.
Example 15
And (3) ball-milling 36wt.% secondary aluminous ash, 40wt.% waste glass, 18wt.% viscosity regulator and 6wt.% foam stabilizer in a mechanical ball mill for 2.7h, setting the ball-milling rotation speed at 420rpm, keeping the mixture at the pressure of 21MPa for 36s, and then keeping the temperature of the pressed sample at 1210 ℃ for 25min to obtain the foamed microcrystalline glass with the porosity of 73% and the compressive strength of 7.11MPa.
While several embodiments of the present invention have been illustrated and described herein, it will be appreciated by those skilled in the art that changes can be made to the embodiments described herein without departing from the spirit of the invention. The above examples are merely illustrative and should not be taken as limiting the scope of the invention.
Claims (5)
1. A method for preparing foam glass ceramics by secondary aluminum ash without pretreatment is characterized in that the foam glass ceramics is obtained by ball milling secondary aluminum ash, waste glass, a viscosity regulator and a foam stabilizer, molding and synchronous foaming crystallization; the waste glass and alumina in secondary aluminum ash slag are used as a silicon source and an aluminum source of a glass network for the foam glass ceramics, the secondary aluminum ash slag is used as a foaming agent, a nucleating agent and a fluxing agent for preparing the foam glass ceramics, the viscosity regulator is used for providing a calcium source for the foam glass ceramics, and the foam stabilizer can change the melt performance of the foam glass ceramics and stabilize the bubble structure; the ball milling technological parameter is ball milling speed of 100-500 rpm for 1-4h, and the heat treatment system of synchronous foaming crystallization is at 1000-1350 ℃ and heat preservation for 20-60 min;
the raw material proportion is 25-40 wt.% of secondary aluminum ash slag, 30-40 wt.% of waste glass, 15-30 wt.% of viscosity regulator and 5-10 wt.% of foam stabilizer; the foam stabilizer is trisodium phosphate.
2. The method for preparing the foam glass-ceramics without the pretreatment of the secondary aluminum ash according to claim 1, wherein the viscosity regulator is one or more of quicklime, calcium carbonate and borax.
3. The method for preparing the foam glass ceramics by the secondary aluminum ash without pretreatment according to claim 1, which comprises the following specific steps:
s1, ball milling: ball-milling secondary aluminum ash, waste glass, a viscosity regulator and a foam stabilizer to obtain a uniform mixture;
s2, forming: pouring the mixture into a mould, and pressing and forming the mixture by using a press;
s3, synchronous foaming and crystallization: and carrying out heat treatment on the raw materials subjected to compression molding to obtain the foam microcrystalline glass.
4. The method for preparing the foam glass-ceramics without the pretreatment of the secondary aluminum ash in claim 3, wherein the mixture is sieved by a 100-mesh sieve after the ball milling.
5. The method for preparing the foam glass-ceramic by using the secondary aluminum ash without pretreatment as claimed in claim 3, wherein the forming parameter is a pressure of 20-30 MPa and a holding time of 20-60 s.
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| CN114620938B (en) * | 2022-03-17 | 2024-03-01 | 河南省高新技术实业有限公司 | Hierarchical porous glass ceramic and preparation method thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1805783A (en) * | 2003-05-16 | 2006-07-19 | 詹姆士·哈代国际金融公司 | Methods for producing low density products |
| CN101274819A (en) * | 2008-02-22 | 2008-10-01 | 中国科学院生态环境研究中心 | Packaged technology for synthesizing foamed glass by using medical refuse incineration residue |
| CN108423997A (en) * | 2018-06-13 | 2018-08-21 | 攀枝花学院 | The method for preparing crystallite foam glass using solid waste |
| CN110436787A (en) * | 2019-09-03 | 2019-11-12 | 济南大学 | A method of foam pyroceram is prepared using solid waste |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102838283B (en) * | 2012-10-11 | 2014-12-17 | 南京师范大学 | Method for producing foam microcrystal glass by utilizing composite industrial residue and product |
| CN107915411A (en) * | 2017-12-18 | 2018-04-17 | 北方工业大学 | A kind of resource utilization method of aluminium ash |
| CN108439809A (en) * | 2018-01-30 | 2018-08-24 | 上海荣丰科技发展有限公司 | Foaming micro crystal material based on smelted furnace cinder and its production technology |
| CN108585519A (en) * | 2018-05-30 | 2018-09-28 | 济南大学 | A method of preparing foam pyroceram using red mud |
| CN108516688A (en) * | 2018-07-03 | 2018-09-11 | 四川名微晶科技股份有限公司 | A method of using aluminium ash be main material production spinel crystallites glass |
| CN110563336A (en) * | 2019-10-23 | 2019-12-13 | 北京科技大学 | Method for preparing microcrystalline glass by aluminum ash without desalting and removing nitrogen |
| CN111362581A (en) * | 2020-03-17 | 2020-07-03 | 吴俊楠 | High-strength foam glass ceramics and preparation method thereof |
-
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1805783A (en) * | 2003-05-16 | 2006-07-19 | 詹姆士·哈代国际金融公司 | Methods for producing low density products |
| CN101274819A (en) * | 2008-02-22 | 2008-10-01 | 中国科学院生态环境研究中心 | Packaged technology for synthesizing foamed glass by using medical refuse incineration residue |
| CN108423997A (en) * | 2018-06-13 | 2018-08-21 | 攀枝花学院 | The method for preparing crystallite foam glass using solid waste |
| CN110436787A (en) * | 2019-09-03 | 2019-11-12 | 济南大学 | A method of foam pyroceram is prepared using solid waste |
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