CN103789797A - Method for producing aluminium-silicon alloy by using pulverized fuel ash - Google Patents
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Abstract
The invention belongs to the field of utilization of pulverized fuel ash resources and metallurgy of aluminum, and provides a method for producing an aluminium-silicon alloy by using pulverized fuel ash. According to the technical scheme, the method comprises the following main steps: (1) uniformly mixing the pulverized fuel ash, recycled smudged materials and washing materials as raw materials, and adding the mixture to an aluminum electrolysis cell instead of a part of aluminium oxide so as to produce the aluminium-silicon alloy, wherein the pulverized fuel ash weighs 0.70+/-0.5 ton and accounts for 10%-30% of the weight of the total raw materials, the recycled smudged materials (various smudged raw materials recycled from electrolytic aluminium factories) weigh 1.2+/-0.3 tons and accounts for 25%-35% of the weight of the total raw materials, the washing materials (materials obtained by flotation of carbon residues fished out from the aluminum electrolysis cell) weigh 1.2+/-0.3 tons and accounts for 25%-35% of the weight of the total raw materials, and the aluminum oxide weighs 0.8+/-0.2 ton and accounts for 10%-30% of the weight of the total raw materials; and (2) adding the mixture and the aluminum oxide to the aluminum electrolysis cell in an aluminum electrolysis cell normal production manner, wherein 1.0-1.6 tons of electrolyte is produced while each 1 ton of aluminium-silicon alloy is produced.
Description
Technical field
The invention belongs to fly ash utilization and metallurgy of aluminium field.
Background technology
For convenience of narration, material title and the molecular formula corresponding relation in literary composition, mentioned are as follows:
1. aluminum oxide (Al
2o
3), silicon oxide (SiO
2), ferric oxide (Fe
2o
3), calcium oxide (CaO).
2. aluminum silicon alloy=al-si-based alloy (that is:, take aluminium silicon as base metal, also containing the alloy of other a small amount of metal).
Flyash is the lime-ash being formed after burning by the fuel such as coal dust, coal slime that discharge in fuel-burning power plant.China is the country take coal as main energy sources, and the flyash of generation is the industrial waste of China's discharge capacity maximum.By in December, 2011, China's electric power entirety installed capacity has reached 10.5 trillion kW, wherein thermoelectricity accounting 72%, thermoelectricity produces approximately 4.5 hundred million tons of flyash amounts every year, along with the sustainable growth of China's economy, thermoelectricity installed capacity also constantly increases, flyash discharge has become the maximum Single Pollution source of Chinese industrial solid waste, in the flyash sample of sampling Detection, detect more than 20 kind to environment and the harmful material of human body, comprising causing nervous system injury, inborn defect is the heavy metal of cancer even, as roughly estimated, China approximately has the cadmium of 2.9 ten thousand tons every year, chromium, arsenic, the heavy metal of mercury and plumbous these five kinds of state key monitoring enters into physical environment with the discharge of flyash, also the concentration that demonstrates multiple harmful substances for the detection of near surface water part Ash field and underground well water has exceeded national relevant criterion, objectionable impurities in flyash unavoidably ground contamination soil around, empty G&W, near not only threatening, resident's is healthy, also can jeopardize larger public group by food chain.At present, total volume of cargo in storage of China's flyash has exceeded 1,000,000,000 tons, and it not only takies a large amount of soils, and also normal discharge rivers, make channel filling, and river is rotten, and serious environment pollution, is therefore important source of pollution.
Through inquiry pertinent data, China's main scope of typical flyash composition is as follows:
| Composition | SiO 2 | Al 2O 3 | Fe 2O 3 | CaO | MgO | SO 2 | Na 2O and K 2O | Loss on ignition |
| Content % | 34～65 | 14～40 | 1～16 | 0～25 | 0～4 | 0～6 | 0.5～4 | 1～26 |
Find out from upper table, in China's flyash, mainly contain silicon oxide (SiO
2), aluminum oxide (Al
2o
3) and the composition such as other metal oxide, therefore the recycling to flyash, can avoid the pollution to environment of the wasting of resources and solid waste, can recycle metal and mineral wherein again, this not only makes disposal of pollutants problem obtain part solution, improve environment, and saved Mineral Resources in China, for China provides another strip metal source channel.
For many years, generally pay attention to the comprehensive utilization of resources of flyash both at home and abroad, fly ash utilization research is divided into basic, normal, high three aspects both at home and abroad at present: low technical is mainly used for flyash the aspects such as the build of dam, road, engineering backfill, soil improvement; Middle technology is mainly used as material of construction by flyash, as produced flyash brick etc.; The applied research of high-tech sector refers to the aspects such as the extraction to flyash mineral or valuable element.From current applicable cases both domestic and external, the application of low, middle technology becomes better and approaching perfection day by day, and obtains lot of research and puts into practice, and high-tech application progress is relatively slow, and in flyash, various useful metals do not obtain fully effectively utilizing as aluminium, silicon etc.
At present, the technological method that utilizes flyash to extract the valuable metals such as aluminium, silicon mainly contains two large classes, is described as follows:
First kind method can be sketched and produce aluminum silicon alloy (note: the Silicon In Alloys content that this method is produced is more for flyash elred process, aluminium content takes second place, therefore also can be described as silumin), method is: after flyash is mixed in proportion, stirred with additive, reductive agent, binding agent, make high-intensity pelletizing, the pelletizing of flyash being made with carbon electrode by ore-smelting furnace again carries out heat reduction smelting, make crude aluminum silicon alloy, send into again refining furnace, remove the gred, be then cast as aluminium-silicon ingots by interpolation refining agent, refining.
First kind method cited paper:
The processing method of extracting aluminium silicon alloy from fly ash, patent No. CN200510017735.6, publication number CN1718807, January 11 2006 publication date.
First kind method main drawback:
1. the state-of-the-art production technology level of this method also can only obtain the thick alloy containing aluminium 65% left and right at present, must could obtain application alloy through refining and allotment.The method of refining having adopted has centrifuging, filtration method, selection dissolution method and dilution method.Former three equipment complexity, technical qualification harshness, latter need consume a large amount of fine aluminiums.
2. high temperature reduction process is wayward, and metal volatilization loss is serious;
3. aluminium content is not high, the limited (note: in flyash, silicone content is usually above aluminium content, and the common silicone content of product that therefore elred process is produced is higher than aluminium content of range of application.)；
4. in aluminum silicon alloy, foreign matter content is many, and product grade is not high.
For example, in the product of the method except containing sial element, also contain iron, calcium and other metal or nonmetallic impurity or oxide compound, product is mainly used in the reductive agent of steel making deoxidant and heat-generating agent or metallothermics refining magnesium, as the silumin of FeAl17Si40, it is that 40.0%, Al is 21.16% that its silicon, aluminium content requirement are respectively Si.
Equations of The Second Kind method is roughly divided into three steps, the first step is to utilize aluminous fly-ash to produce aluminum oxide (note: aluminum oxide is the main raw material of electrolytic aluminum), second step is produced electrolytic aluminum with aluminum oxide by electrolytic process, the 3rd step is mixed with aluminum silicon alloy with mix-melting method by add Pure Silicon Metal in aluminium liquid, mainly the first step owing to relating to the technology of utilization of fly ash, therefore below, only the first step method is described, the first step method is summed up as following two kinds of methods:
The 1st kind of method is referred to as alkaline process: this method is similar to the current method with bauxite production metallurgy grade aluminum oxide, and master operation flow process is: flyash and Wingdale mixing, sintering, pre-desiliconizing, add caustic alkali (that is: sodium hydroxide), High Temperature High Pressure stripping, desiliconization, settlement separate, seed decomposition, roasting becomes aluminum oxide.There is the main drawbacks such as Production Flow Chart is long, energy consumption is high, supplies consumption is many, production cost is high, waste amount is large in this method, is worth little from economy.
The 2nd kind of method is referred to as acid system: by acid adding by the alumina dissolution in flyash, silicon oxide does not dissolve or indissoluble solution, then will become filter cake containing aluminic acid solution filter, filter cake is produced aluminum oxide through calcining, this kind of method flow is shorter than alkaline process, economy is good compared with alkaline process, but exist other foreign metal and enter solution with aluminium, affect alumina product purity, acid-resistant system high cost (has expert's Vivid analogy: acid system extracts aluminium, the acid-resistant system and the pipeline that use rare earth tantalum-niobium alloy to make, investment meeting is large to being unable to estimate, nor real, tantalum niobium resource is so few, make thick pipe, remove to produce cheap aluminum oxide, like building a golden passage way, but be used for transporting rubbish), the pollution that in production process, acid brings is difficult for the main bugbears such as solution, for example: use gas washing in SA production aluminum oxide effect not use hydrochloric acid good, production process needs airtight, enter atmosphere and can cause acid rain in atmosphere, using the sealing of hydrochloric acid in whole production process is a serious problem, once there will be to the serious consequence of people's death because the chlorine producing in production process leaks, can can produce major hidden danger to environment.
Equations of The Second Kind method cited paper: the thinking " the 1st phase of light metal 2010 " of 1. aluminous fly-ash being produced aluminum oxide technology and Industrialized processing technique route; 2. the present Research take flyash as raw material production aluminum oxide and silica gel " light metal 2011 o. 11ths "; 3. the research and development of aluminous fly-ash full resource utilization technology " the 9th phase of light metal 2012 "; 4. the research of pre-desiliconizing with high alumina fly ash process optimization " the 7th phase of light metal 2013 "; 5. aluminium oxide extraction process from coal ash progress " light metal 2013 o. 11ths ".
The main drawback of Equations of The Second Kind method:
1. from flyash → aluminum oxide → aluminium → aluminum silicon alloy angle, total Production Flow Chart is long, (for example: say frankly according to the chairman Wang Shuen of China Huadian Corporation cause that social gross investment is large, production cost is high, only extract aluminum oxide cost with regard to flyash, ratio alumyte extracts aluminum oxide and exceeds three or five hundred yuan);
2. such production method optionally by alumina extraction less composition in flyash out, and a large amount of other compositions in flyash are discharged as impurity, cause producing the waste red mud amount that aluminum oxide produces too large, and the another kind of a large amount of metallurgical slag of formation, increase Environmental Protection in China pressure, in order to reduce waste red mud residues amount, must the large-scale jointly producing cement of auxiliary construction factory (for example: former Chalco Zhengzhou research institute president Li Wangxing says: according to this technique, 1 ton of aluminum oxide of every refinement, need to consume 3～3.5 tons of aluminous fly-ashs, consume 8 tons of Wingdales, finally produce 10 tons of waste red mud residues, the alumina producer of such 400,000 tons, need the cement mill of supporting 4,000,000 tons, could consume these waste residues, say utilization of waste material, actual is that refuse rolls larger and larger),
3. in flyash, the silicon oxide of one of main oxides is separated and wastes, if will extract silicon oxide, also needs separately to add Production Flow Chart, causes flow process longer, and cost is higher.In these class methods, there is certain methods that the materials such as the silicon oxide of separating are extracted and produce white carbon black (note: white carbon black is the general name of white powder X ray amorphous silicic acid and silicate product);
4. the aluminous fly-ash resource-constrained of China, is mainly distributed in Inner Mongol, Shanxi and North Shaanxi, and therefore this technology is subject to certain limitation in China's application.
Summary of the invention
1. goal of the invention
For utilizing at present flyash to extract the existing problem of two large class technological methods of the valuable metals such as aluminium, silicon, the present invention looks for another way, having proposed one utilizes flyash to produce aluminum silicon alloy method, both: replace a part of aluminum oxide directly to join the method for producing aluminum silicon alloy in aluminium cell with flyash, the problem that the present invention can avoid current two large class fly ashs to utilize method to exist.
Main thought of the present invention is: in flyash, mainly contain silicon oxide (SiO
2), aluminum oxide (Al
2o
3), wherein: aluminum oxide is the main raw material of aluminium cell, silicon oxide can become Pure Silicon Metal by electrolysis or by aluminium reducing in aluminium cell, other a small amount of various metal oxides also can become metal by electrolysis or by aluminium reducing, also some oxide compound is as calcium oxide or the useful subsidiary material of Aluminium Electrolysis, and it is feasible therefore flyash being added to the thinking of producing al-si-based alloy in aluminium cell.And adopt at present flyash to add the method for producing al-si-based alloy in aluminium cell not to be seen in report.
2. technical scheme
Technical solution of the present invention is as follows:
1. take flyash, reclaim dirty material, washing material and in aluminium cell, produce al-si-based alloy as raw material (hereinafter to be referred as compound) after mixing replaces a part of aluminum oxide (note: the main raw material of aluminium cell) to join, according to the composition difference of three kinds of raw materials, calculate by producing 1 ton of al-si-based alloy, required three kinds of raw material consumptions are as follows:
0.70 ± 0.5 ton, flyash, accounts for 10%～30% of total raw material amount, flyash Contents of Main Components: Al
2o
3be 16%～50%, SiO
2be 33%～60%.
Reclaim 1.2 ± 0.3 tons, dirty material, account for 25%～35% of total raw material amount, reclaiming dirty material is the various raw materials of making dirty that reclaim from electrolytic aluminium factory, reclaims dirty material Contents of Main Components: Al
2o
3be 35%～50%, ionogen is 35%～55%.
1.2 ± 0.3 tons, washing material, accounts for 25%～35% of total raw material amount, and washing material is the breeze pulled out from the aluminium cell material through floatingly selecting, washing material Contents of Main Components: Al
2o
3be 6%～10%, ionogen is 65%～75%.
Above three kinds of raw materials become compound after mixing, and compound accounts for 70%～90% of total stuff amount.
All the other raw materials that account for total stuff amount 10%～30% are aluminum oxide, and aluminum silicon alloy per ton needs 0.8 ± 0.2 ton, aluminum oxide.
2. with the normal mode of production of aluminium cell, compound and aluminum oxide are added in aluminium cell and produce al-si-based alloy, often producing 1 ton of al-si-based alloy simultaneously, also can produce 1.0～1.6 tons of byproduct ionogen.
Note: dissolved oxygen aluminium the reaction medium (selecting from " modern aluminum electrolysis ") that is metallic aluminium it through electrolytic reduction when ionogen is electrolysis of aluminum, the ionogen of aluminium cell is mainly various fluorine-containing materials.
3. the technology of the present invention compared with the prior art
At present, approach prior art of the present invention most and mainly contain two classes:
First kind method can be sketched and produce aluminum silicon alloy for flyash elred process, this class methods main drawback: 1. the state-of-the-art production technology level of this method also can only obtain the thick alloy containing aluminium 65% left and right at present, must could obtain application alloy through refining and allotment.The method of refining having adopted has centrifuging, filtration method, selection dissolution method and dilution method.Former three equipment complexity, technical qualification harshness, latter need consume a large amount of fine aluminiums.2. high temperature reduction process is wayward, and metal volatilization loss is serious; 3. aluminium content is not high, and range of application is limited; 4. in aluminum silicon alloy, foreign matter content is many, and product grade is not high.
Equations of The Second Kind method is to utilize aluminous fly-ash to produce aluminum oxide and then produce aluminum silicon alloy, the main drawback of these class methods: 1. from flyash → aluminum oxide → aluminium → aluminum silicon alloy angle, total long flow path, causes that social gross investment is large, production cost is high; 2. due to optionally only by alumina extraction in flyash, cause the waste red mud amount that produces too large, and form another kind of a large amount of metallurgical slag, increase Environmental Protection in China pressure, in order to reduce waste red mud residues amount, must the large-scale jointly producing cement of auxiliary construction factory; 3. in flyash, the silicon oxide of one of main oxides is separated and wastes, if will extract silicon oxide, also needs separately to add Production Flow Chart, causes flow process longer, and cost is higher; 4. the aluminous fly-ash resource-constrained of China, is mainly distributed in Inner Mongol, Shanxi and North Shaanxi, and therefore such technology application is limited.
Compare above two class technology, advantage of the present invention is as follows:
1. for fly ash efficiently utilizes, a broad space has been proposed, easy to implement and take effect: China is Aluminum Electrolysis Production big country, produce about 2,000 ten thousand tons of electrolytic aluminum per year, electrolytic aluminum output accounts for the more than 40% of Gross World Product, the present invention implements on aluminium cell, do not change electrolytic aluminium production process flow process, easy to implement and take effect, for utilization of fly ash provides broad space.
2. aluminum oxide, silicon oxide, ionogen resource and other valuable metal resource of some amount have been saved: China produces about 2,000 ten thousand tons of electrolytic aluminum per year, electrolytic aluminum per ton need consume about 2 tons of aluminum oxide, calculate by silicon oxide-containing 45% in salic 25% in 20% substitution rate, flyash, flyash with coal ash instead aluminum oxide, adopt flyash year to save approximately 2,000,000 tons of alumina resources, approximately 3,600,000 tons of year saving silicon oxide resources; In addition in reclaim dirty material instead of alumina by 30% substitution rate, reclaim in dirty material salicly 40%, adopt and reclaim dirty material year and save approximately 4,800,000 tons of alumina resources; In addition in washing material instead of alumina by salic 10% in 30% substitution rate, washing material, adopt washing material year to save approximately 1,200,000 tons of alumina resources.Add up to year 8000000 tons of alumina resources of saving, save 3,600,000 tons of silicon oxide resources.
3. effectively protected environment; avoid secondary pollution: this project is directly eaten flyash dry bleeding; produce with China that about 2,000 ten thousand tons of electrolytic aluminum, electrolytic aluminum per ton need consume about 2 tons of aluminum oxide, coal ash instead aluminum oxide calculates by 20% substitution rate per year, year consume about 8,000,000 tons of flyash.The present invention also eats dry bleeding by the breeze the like waste of pulling out in dirty the recovery of electrolytic aluminium factory material, aluminium cell in consuming flyash, for example, calculate by 30% substitution rate to reclaim dirty material instead of alumina, and 1,200 ten thousand tons, dirty material is reclaimed in year consumption.In addition the present invention can not resemble flyash and produce aluminum oxide method generation red mud the like waste, can not resemble flyash yet and produce silumin method generation sial slag the like waste, so that environment is caused to secondary pollution.
4. flow process is short, cost is low: adopt flyash or pretreated flyash are added on to direct production aluminum silicon alloy in aluminium cell, flow process is short, cost is low, avoid walking the detour that flyash is produced aluminum oxide and then produced aluminum silicon alloy, reduce total social investment, saved society human, material resources and financial resources;
5. superior product quality, aluminum content is high: the silumin that the aluminum silicon alloy quality that in aluminium cell, electrolysis goes out is produced than elred process is good: when aluminium cell is produced, raw material is dispersed in the protective layer on al-si-based alloy liquid top in electrolyzer burner hearth, al-si-based alloy liquid is positioned at the burner hearth bottom region of aluminium cell, the each alloying element in this region out forms aluminium alloy with the common precipitating of atom form, owing to being coated with thicker protective layer on al-si-based alloy liquid, make it avoid contacting with air, therefore reduced the hydrogen－sucking amount in aluminium alloy, reduce the secondary scaling loss such as oxidation and volatilization, avoid mixing non-uniform phenomenon, this external protection has the ability of strong dissolved oxygen compound, can avoid occurring in al-si-based alloy oxide inclusion.So this project can improve alloy mass, because coal ash instead amount ratio is less, in the al-si-based alloy that therefore the present invention produces, the content of aluminium is higher than elred process.
In sum, the inventive method, when fly ash deep development is utilized, has been saved the resource such as aluminum oxide, silicon oxide, and Production Flow Chart is simultaneously shorter, and better economy, reaches and turn waste into wealth, improve environment and the comprehensive object of resources conservation.
Embodiment
The present invention is easy to implement, is exemplified below:
First by flyash, reclaim dirty material, washing material assay, sort out and deposit by the difference of various component contents, to calculate to the addition in aluminium cell according to al-si-based alloy product requirement; Then with the normal mode of production of aluminium cell, compound and aluminum oxide are joined in aluminium cell, in producing al-si-based alloy per ton, also produce 1.0～1.6 tons of ionogen of byproduct.Take the flyash of following certain component content, reclaim dirty material, washing material and carry out calculation specifications by 1 ton of al-si-based alloy of every production, 1.2 tons of ionogen as example:
Flyash 700kg, main component: Al
2o
3be 30%, SiO
2be 45%;
Reclaim dirty material 1200kg, main component: Al
2o
3be 40%, ionogen is 45%;
Washing material 1200kg, main component amount: Al
2o
3be 10%, ionogen is 70%;
The another aluminum oxide 800kg that adds.
At present with aluminum oxide (Al
2o
3) for the unit consumption of raw material production electrolytic aluminum be: 1.920 tons of aluminum oxide/ton aluminium.
Press silicon oxide (SiO
2) the molecular formula theoretical unit consumption that calculates silicon is 2.143 tons of silicon oxide/ton silicon, considers active loss, the effective unit consumption of silicon is adjusted into 2.160 tons of silicon oxide/ton silicon.
Be calculated as follows:
1. alumina amount in flyash: 700 × 30%=210kg
2. reclaim alumina amount in dirty material: 1200 × 40%=480kg
3. alumina amount: 1200 × 10%=120kg in washing material
4. the another alumina amount adding: 800kg
5. add up to alumina amount: 210+480+120+800=1610kg
6. the aluminium amount that aluminium cell electrolysis produces: 1610 ÷ 1.92=838.5kg
The silicon amount of 7. producing in flyash: 700 × 45% ÷ 2.16=145.8kg
8., in al-si-based alloy per ton, aluminium, silicone content are respectively: 83.85%, 14.58%
9. al-si-based alloy per ton is saved aluminum oxide: 210+480+120=810kg
10. al-si-based alloy per ton is saved silicon oxide: 700 × 45%=315kg
Show by above calculating, to adding flyash 700kg in aluminium cell, reclaim dirty material 1200kg, washing material 1200kg, aluminum oxide 800kg, can obtain the al-si-based alloy of 1000kg containing aluminium 83.85%, silicon 14.58%, output byproduct 1200kg ionogen in addition, and flyash, 1200kg that al-si-based alloy product per ton consumes 700kg reclaim dirty material, 1200kg washes material, save silicon oxide resource 315kg simultaneously, save alumina resource 810kg etc.
Above-mentioned implementation example is only for describing enforcement of the present invention, its data and method of calculation do not form the restriction to claim scope, other substantial equivalence data or the method for calculation that it may occur to persons skilled in the art that, all within the scope of the claims in the present invention.
Claims (8)
1. utilize flyash to produce an aluminum silicon alloy method, it is characterized in that, take flyash, reclaim dirty material, washing material and produce al-si-based alloy in aluminium cell as raw material replaces a part of aluminum oxide to join after mixing.
2. a kind of fly ash according to claim 1 utilizes method, it is characterized in that, flyash consumption is 0.70 ± 0.5 ton of/ton of aluminum silicon alloy, accounts for 10%～30% of total raw material amount.
3. a kind of fly ash according to claim 1 utilizes method, it is characterized in that, flyash Contents of Main Components is: Al
2o
3be 16%～50%, SiO
2be 33%～60%.
4. a kind of fly ash according to claim 1 utilizes method, it is characterized in that, reclaiming dirty material consumption is 1.2 ± 0.3 tons of/ton of aluminum silicon alloys, accounts for 25%～35% of total raw material amount, and reclaiming dirty material is the various raw materials of making dirty that reclaim from electrolytic aluminium factory.
5. a kind of fly ash according to claim 1 utilizes method, it is characterized in that, reclaims dirty material Contents of Main Components to be: Al
2o
3be 35%～50%, ionogen is 35%～55%.
6. a kind of fly ash according to claim 1 utilizes method, it is characterized in that, washing material consumption is 1.2 ± 0.3 tons of/ton of aluminum silicon alloys, accounts for 25%～35% of total raw material amount, and washing material is the breeze pulled out from the aluminium cell material through floatingly selecting.
7. a kind of fly ash according to claim 1 utilizes method, it is characterized in that, washing material Contents of Main Components is: Al
2o
3be 6%～10%, ionogen is 65%～75%.
8. a kind of fly ash according to claim 1 utilizes method, it is characterized in that, with the normal mode of production of aluminium cell, compound and aluminum oxide are added to and in aluminium cell, produce al-si-based alloy, often producing 1 ton of al-si-based alloy simultaneously, also can produce 1.0～1.6 tons of byproduct ionogen.
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| CN105543902A (en) * | 2016-02-25 | 2016-05-04 | 周俊和 | Technology for producing alloy aluminum inside aluminum cell |
| CN109913911A (en) * | 2019-04-11 | 2019-06-21 | 中南大学 | The processing method of alumina-silica solid waste in a kind of aluminum cell waste liner |
| CN111005038A (en) * | 2019-12-10 | 2020-04-14 | 中南大学 | Preparation method of aluminum-silicon-iron alloy |
| CN112725842A (en) * | 2020-12-28 | 2021-04-30 | 郑州大学 | Method for preparing aluminum-silicon-based alloy by using fly ash |
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| CN109913911A (en) * | 2019-04-11 | 2019-06-21 | 中南大学 | The processing method of alumina-silica solid waste in a kind of aluminum cell waste liner |
| CN111005038A (en) * | 2019-12-10 | 2020-04-14 | 中南大学 | Preparation method of aluminum-silicon-iron alloy |
| CN111005038B (en) * | 2019-12-10 | 2021-03-26 | 中南大学 | Preparation method of aluminum-silicon-iron alloy |
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