CN103966452B - A kind of recoverying and utilizing method of the magnesium alloy scrap containing aluminium - Google Patents
A kind of recoverying and utilizing method of the magnesium alloy scrap containing aluminium Download PDFInfo
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- 229910052782 aluminium Inorganic materials 0.000 title claims abstract description 85
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 title claims abstract description 85
- 229910000861 Mg alloy Inorganic materials 0.000 title claims abstract description 68
- 238000000034 method Methods 0.000 title claims abstract description 47
- 239000004411 aluminium Substances 0.000 title claims 16
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical group [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims abstract description 58
- 238000003723 Smelting Methods 0.000 claims abstract description 35
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 23
- 230000008018 melting Effects 0.000 claims abstract description 22
- 238000002844 melting Methods 0.000 claims abstract description 21
- 239000011777 magnesium Substances 0.000 claims abstract description 19
- 238000004064 recycling Methods 0.000 claims abstract description 18
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 16
- 238000007872 degassing Methods 0.000 claims abstract description 14
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 13
- 239000000956 alloy Substances 0.000 claims abstract description 13
- 239000000155 melt Substances 0.000 claims abstract description 11
- 238000007670 refining Methods 0.000 claims abstract description 11
- 239000007788 liquid Substances 0.000 claims description 28
- 238000003756 stirring Methods 0.000 claims description 21
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 18
- 239000001257 hydrogen Substances 0.000 claims description 18
- 229910052739 hydrogen Inorganic materials 0.000 claims description 18
- 238000007731 hot pressing Methods 0.000 claims description 17
- 238000003825 pressing Methods 0.000 claims description 11
- 239000007789 gas Substances 0.000 claims description 10
- 238000007664 blowing Methods 0.000 claims description 7
- 238000001035 drying Methods 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 6
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 4
- 229910052751 metal Inorganic materials 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims description 4
- 239000011780 sodium chloride Substances 0.000 claims description 2
- 229910001051 Magnalium Inorganic materials 0.000 claims 3
- 238000009997 thermal pre-treatment Methods 0.000 claims 3
- 238000010792 warming Methods 0.000 claims 3
- 239000002699 waste material Substances 0.000 abstract description 35
- SNAAJJQQZSMGQD-UHFFFAOYSA-N aluminum magnesium Chemical compound [Mg].[Al] SNAAJJQQZSMGQD-UHFFFAOYSA-N 0.000 abstract description 22
- 238000004519 manufacturing process Methods 0.000 abstract description 13
- 238000005266 casting Methods 0.000 abstract description 9
- 238000011084 recovery Methods 0.000 abstract description 7
- 230000001681 protective effect Effects 0.000 abstract description 3
- 239000002893 slag Substances 0.000 abstract description 3
- 230000003647 oxidation Effects 0.000 abstract description 2
- 238000007254 oxidation reaction Methods 0.000 abstract description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 6
- 238000005238 degreasing Methods 0.000 description 5
- 230000008929 regeneration Effects 0.000 description 4
- 238000011069 regeneration method Methods 0.000 description 4
- 229910052786 argon Inorganic materials 0.000 description 3
- 230000004907 flux Effects 0.000 description 3
- 238000004821 distillation Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 238000011112 process operation Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 229910004261 CaF 2 Inorganic materials 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000013016 damping Methods 0.000 description 1
- 238000004512 die casting Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001192 hot extrusion Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
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- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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Abstract
一种含铝的镁合金废屑的回收利用方法,本发明涉及镁合金废屑的回收利用方法,具体涉及利用含铝的镁合金废屑制备铝镁中间合金的方法,它要解决含铝的镁合金在生产加工过程中产生的废屑回收利用率低的问题。镁合金废屑回收方法:一、镁合金废屑热压成镁件;二、熔化铝锭条;三、向铝液中钟罩压入部分的镁件进行熔炼;四、再加入剩余的镁件,熔炼得到铝镁液;五、加入熔炼剂对熔体进行精炼;六、除气后撇渣,浇铸成锭得到铝镁中间合金。本发明镁合金废屑的回收利用过程不需要保护气氛,镁合金在高温下氧化烧损减少,生产工艺简单,采用镁合金废屑降低生产成本,并可使镁元素的回收利用率达到90%以上。A method for recycling aluminum-containing magnesium alloy waste, the invention relates to a recycling method for magnesium alloy waste, in particular to a method for preparing aluminum-magnesium master alloys from aluminum-containing magnesium alloy waste, which solves the problem of aluminum-containing The problem of low recycling rate of waste chips generated during the production and processing of magnesium alloys. Magnesium alloy waste recovery method: 1. Magnesium alloy waste is hot pressed into magnesium parts; 2. Aluminum ingot is melted; 3. Magnesium parts are pressed into the molten aluminum bell jar for smelting; 4. Add the remaining magnesium 5. Refining the melt by adding a melting agent; 6. Skimming the slag after degassing, and casting it into an ingot to obtain an aluminum-magnesium master alloy. The recycling process of the magnesium alloy waste in the present invention does not require a protective atmosphere, the oxidation and burning loss of the magnesium alloy is reduced at high temperature, the production process is simple, the use of the magnesium alloy waste reduces the production cost, and the recycling rate of the magnesium element can reach 90%. above.
Description
技术领域technical field
本发明涉及镁合金废屑的回收利用方法,具体涉及利用含铝的镁合金废屑制备铝镁中间合金的方法。The invention relates to a method for recycling magnesium alloy waste, in particular to a method for preparing an aluminum-magnesium master alloy by using aluminum-containing magnesium alloy waste.
背景技术Background technique
镁合金具有密度低、比强度和比刚度高、热传导性能好、阻尼减振降噪性佳、液态成型性能优越、机械加工性能优良、电磁屏蔽能力强等优点,表现出极其重要的使用价值和广阔的应用前景,适合于汽车、摩托车、计算机、通讯、仪器仪表、家电、轻工、军事等行业。Magnesium alloy has the advantages of low density, high specific strength and specific stiffness, good thermal conductivity, good damping, vibration and noise reduction, excellent liquid forming performance, excellent machining performance, strong electromagnetic shielding ability, etc., showing extremely important use value and Broad application prospects, suitable for automobiles, motorcycles, computers, communications, instrumentation, home appliances, light industry, military and other industries.
镁合金按成形工艺分为铸造镁合金和变形镁合金,变形镁合金以AZ31镁合金为代表,具有良好的延展性和中等高强度,且价格便宜,是目前商业化应用最普遍的变形镁合金;铸造镁合金以AZ91镁合金为代表,具有较高的强度和优异的铸造性能。但是镁合金在生产加工过程中使用率不高,例如AZ91镁合金采用压力铸造工艺生产,从生产原料到成品的材料利用率不足50%,产生大量的废料,如何回收利用这些废料受到人们广泛的重视。Magnesium alloys are divided into cast magnesium alloys and wrought magnesium alloys according to the forming process. Wrought magnesium alloys are represented by AZ31 magnesium alloys, which have good ductility, medium and high strength, and are cheap. They are currently the most common wrought magnesium alloys in commercial applications. ; Cast magnesium alloy is represented by AZ91 magnesium alloy, which has high strength and excellent casting performance. However, the utilization rate of magnesium alloys in the production and processing process is not high. For example, AZ91 magnesium alloy is produced by die casting process, and the material utilization rate from production raw materials to finished products is less than 50%, resulting in a large amount of waste. How to recycle these wastes is widely discussed by people. Pay attention to.
目前镁合金废料可通过固相再生和液相再生进行回收。固相再生是基于热压或热挤工艺直接成形,这种方法较新,技术不成熟,处于实验室研究阶段。液相再生包括蒸馏法、坩埚炉法、盐浴槽法、双炉法、无熔剂吹氩过滤精练法和隔室气体吹泡法,蒸馏法是基于各元素蒸气压不同的原理进行真空提纯,适合于纯镁,所用的设备成本较高,操作复杂,能耗大;坩埚炉法采用熔剂保护直接加热镁合金废料,熔剂易残留在金属液中,产生内部熔剂夹杂,降低产品质量,在熔炼过程中会放出有害的Cl2或HCl气体;盐浴槽法和双炉法可将镁合金液逐步净化或将熔化炉和浇铸炉分开,熔炼时采用SF6气氛进行保护,是目前镁合金废料回收利用的主要方法;无熔剂吹氩过滤精练法和隔室气体吹泡法基于对熔融的镁合金液搅拌的同时,在熔池底部吹入氩气,产生细小气泡对熔体起搅拌作用,促进杂质分离,工艺操作时间较长,成本较高,较少应用于工业生产中。At present, magnesium alloy waste can be recycled through solid-phase regeneration and liquid-phase regeneration. Solid phase regeneration is based on hot pressing or hot extrusion process direct forming, this method is relatively new, the technology is immature, and it is in the stage of laboratory research. Liquid phase regeneration includes distillation method, crucible furnace method, salt bath method, double furnace method, flux-free argon blowing filtration refining method and compartment gas blowing method. Distillation method is based on the principle of different vapor pressure of each element for vacuum purification, suitable for For pure magnesium, the cost of the equipment used is high, the operation is complicated, and the energy consumption is large; the crucible furnace method uses flux protection to directly heat the magnesium alloy scrap, and the flux is easy to remain in the molten metal, resulting in internal flux inclusions and reducing product quality. Harmful Cl 2 or HCl gas will be released in the process; the salt bath method and the double furnace method can gradually purify the magnesium alloy liquid or separate the melting furnace and the casting furnace. SF 6 atmosphere is used for protection during smelting. The main method; the flux-free argon blowing filtration refining method and the compartment gas blowing bubble method are based on stirring the molten magnesium alloy liquid while blowing argon gas at the bottom of the molten pool to generate fine bubbles to stir the melt and promote impurities. Separation, the process operation time is longer, the cost is higher, and it is rarely used in industrial production.
由于镁合金在高温下氧化烧损严重,熔炼浇铸过程中必须采用保护措施,工艺比较复杂且工艺操作时间较长,同时大量的镁残留在废渣中,镁合金废料的回收利用率较低。Because magnesium alloys are severely oxidized and burned at high temperatures, protective measures must be taken during the melting and casting process. The process is relatively complicated and the process operation time is long. At the same time, a large amount of magnesium remains in the waste residue, and the recycling rate of magnesium alloy waste is low.
发明内容Contents of the invention
本发明目的是为了解决含铝的镁合金在生产加工过程中产生的废屑回收利用率低的问题,而提供一种含铝的镁合金废屑的回收利用方法。The purpose of the present invention is to solve the problem of low recycling rate of waste chips generated during the production and processing of aluminum-containing magnesium alloys, and to provide a method for recycling waste chips of aluminum-containing magnesium alloys.
本发明含铝的镁合金废屑的回收利用方法按下列步骤实现:The recycling method of the aluminum-containing magnesium alloy waste chips of the present invention is realized in the following steps:
一、将生产加工中产生的含铝的镁合金废屑除油后烘干,然后把烘干的镁合金废屑在压力机上热压制成镁件;1. Degreasing and drying the aluminum-containing magnesium alloy waste generated during production and processing, and then hot-pressing the dried magnesium alloy waste on a press to make magnesium parts;
二、依照化学式AlMgn,n为1≦n≦20,按化学计量比称取铝锭条和镁件,沿着熔炼炉的炉壁排列铝锭条,开启熔炼炉熔化铝锭条,然后均匀撒上经预热处理后的熔炼剂,得到铝液;2. According to the chemical formula AlMgn, n is 1≦n≦20, weigh the aluminum ingots and magnesium parts according to the stoichiometric ratio, arrange the aluminum ingots along the furnace wall of the melting furnace, open the melting furnace to melt the aluminum ingots, and then spread them evenly Add the preheated smelting agent to obtain molten aluminum;
三、将铝液升温至740~760℃,采用钟罩压入式加入所需镁件质量的1/3~1/2,待镁件全部熔化后停炉,以5~20cm/s的速度搅拌2~3分钟,得到含镁的铝液;3. Raise the temperature of the molten aluminum to 740-760°C, add 1/3-1/2 of the mass of the required magnesium parts by pressing the bell jar, and stop the furnace after all the magnesium parts are melted, at a speed of 5-20cm/s Stir for 2 to 3 minutes to obtain aluminum liquid containing magnesium;
四、将熔炼炉升温至740~760℃,采用钟罩压入式加入剩余的镁件,待镁件全部熔化后停炉,以5~20cm/s的速度搅拌2~3分钟,得到铝镁液;4. Raise the temperature of the smelting furnace to 740-760°C, add the remaining magnesium parts by pressing the bell jar, stop the furnace after all the magnesium parts are melted, and stir for 2-3 minutes at a speed of 5-20cm/s to obtain aluminum-magnesium liquid;
五、熔炼炉升温至740~760℃,在铝镁液表面均匀加入经预热处理后的熔炼剂对熔体进行精炼,同时以5~20cm/s的速度均匀搅拌,精炼时间为5~10分钟,静置5~10分钟后撇渣,得到熔融铝液;5. Heat up the smelting furnace to 740-760°C, evenly add the preheated smelting agent to the surface of the aluminum-magnesium liquid to refine the melt, and at the same time stir evenly at a speed of 5-20cm/s, and the refining time is 5-10 Minutes, after standing for 5-10 minutes, skimming to obtain molten aluminum liquid;
六、在步骤五的熔融铝液温度为720~730℃的条件下,利用旋转除气机使用N2与Cl2的混合气体进行除气处理,利用测氢仪测量氢含量,当氢含量达到0.2ml/100gAl以下时,停止除气静置10~15分钟后撇渣,然后再在熔融铝液温度为700~730℃时进行撇渣浇铸成锭,得到铝镁中间合金,完成含铝的镁合金废屑的回收利用。6. Under the condition that the molten aluminum temperature in step 5 is 720-730°C, use a rotary degasser to use a mixed gas of N 2 and Cl 2 for degassing treatment, and use a hydrogen detector to measure the hydrogen content. When the hydrogen content reaches When it is below 0.2ml/100gAl, stop degassing and let it stand for 10-15 minutes before skimming, and then skimming and casting into ingots when the temperature of molten aluminum is 700-730°C to obtain an aluminum-magnesium master alloy and complete aluminum-containing Recycling of magnesium alloy scrap.
本发明含铝的镁合金废屑的回收利用方法与现有回收利用镁合金废屑工艺相比,熔炼浇铸过程所用设备简单,不需要保护气氛,镁合金在高温下氧化烧损减少,生产工艺简单,同时采用镁合金废屑,生产成本显著降低。Compared with the existing process for recycling magnesium alloy waste, the method for recycling aluminum-containing magnesium alloy waste in the present invention has simple equipment used in the smelting and casting process, does not require a protective atmosphere, and reduces oxidation and burning of the magnesium alloy at high temperatures. Simple, while using magnesium alloy waste chips, the production cost is significantly reduced.
本发明回收利用含铝的镁合金废屑方法的优点在于将生产加工过程中产生的废弃镁合金屑重新利用,同时制造出价格相对较低而且质量合格的铝镁中间合金,可使镁元素的回收利用率达到90%以上。The advantage of the method for recycling aluminum-containing magnesium alloy scraps of the present invention is that the discarded magnesium alloy scraps produced during the production process can be reused, and at the same time, a relatively low price and qualified aluminum-magnesium master alloy can be produced, which can make the magnesium element The recycling rate reaches more than 90%.
具体实施方式Detailed ways
具体实施方式一:本实施方式含铝的镁合金废屑的回收利用方法按下列步骤实施:Specific implementation mode one: the recycling method of the aluminum-containing magnesium alloy waste of the present implementation mode is implemented according to the following steps:
一、将生产加工中产生的含铝的镁合金废屑除油后烘干,然后把烘干的镁合金废屑在压力机上热压制成镁件;1. Degreasing and drying the aluminum-containing magnesium alloy waste generated during production and processing, and then hot-pressing the dried magnesium alloy waste on a press to make magnesium parts;
二、依照化学式AlMgn,n为1≦n≦20,按化学计量比称取铝锭条和镁件,沿着熔炼炉的炉壁排列铝锭条,开启熔炼炉熔化铝锭条,然后均匀撒上经预热处理后的熔炼剂,得到铝液;2. According to the chemical formula AlMgn, n is 1≦n≦20, weigh the aluminum ingots and magnesium parts according to the stoichiometric ratio, arrange the aluminum ingots along the furnace wall of the melting furnace, open the melting furnace to melt the aluminum ingots, and then spread them evenly Add the preheated smelting agent to obtain molten aluminum;
三、将铝液升温至740~760℃,采用钟罩压入式加入所需镁件质量的1/3~1/2,待镁件全部熔化后停炉,以5~20cm/s的速度搅拌2~3分钟,得到含镁的铝液;3. Raise the temperature of the molten aluminum to 740-760°C, add 1/3-1/2 of the mass of the required magnesium parts by pressing the bell jar, and stop the furnace after all the magnesium parts are melted, at a speed of 5-20cm/s Stir for 2 to 3 minutes to obtain aluminum liquid containing magnesium;
四、将熔炼炉升温至740~760℃,采用钟罩压入式加入剩余的镁件,待镁件全部熔化后停炉,以5~20cm/s的速度搅拌2~3分钟,得到铝镁液;4. Raise the temperature of the smelting furnace to 740-760°C, add the remaining magnesium parts by pressing the bell jar, stop the furnace after all the magnesium parts are melted, and stir for 2-3 minutes at a speed of 5-20cm/s to obtain aluminum-magnesium liquid;
五、熔炼炉升温至740~760℃,在铝镁液表面均匀加入经预热处理后的熔炼剂对熔体进行精炼,同时以5~20cm/s的速度均匀搅拌,精炼时间为5~10分钟,静置5~10分钟后撇渣,得到熔融铝液;5. Heat up the smelting furnace to 740-760°C, evenly add the preheated smelting agent to the surface of the aluminum-magnesium liquid to refine the melt, and at the same time stir evenly at a speed of 5-20cm/s, and the refining time is 5-10 Minutes, after standing for 5-10 minutes, skimming to obtain molten aluminum liquid;
六、在步骤五的熔融铝液温度为720~730℃的条件下,利用旋转除气机使用N2与Cl2的混合气体进行除气处理,利用测氢仪测量氢含量,当氢含量达到0.2ml/100gAl以下时,停止除气静置10~15分钟后撇渣,然后再在熔融铝液温度为700~730℃时进行撇渣浇铸成锭,得到铝镁中间合金,完成含铝的镁合金废屑的回收利用。6. Under the condition that the molten aluminum temperature in step 5 is 720-730°C, use a rotary degasser to use a mixed gas of N 2 and Cl 2 for degassing treatment, and use a hydrogen detector to measure the hydrogen content. When the hydrogen content reaches When it is below 0.2ml/100gAl, stop degassing and let it stand for 10-15 minutes before skimming, and then skimming and casting into ingots when the temperature of molten aluminum is 700-730°C to obtain an aluminum-magnesium master alloy and complete aluminum-containing Recycling of magnesium alloy scrap.
本实施方式步骤二均匀撒上经预热处理后的熔炼剂以减少铝液的烧损。Step 2 of this embodiment evenly sprinkles the preheated smelting agent to reduce the burning loss of the molten aluminum.
本实施方式步骤二和步骤五中熔炼剂的使用量为金属熔体重量的0.5%~0.8%,步骤二中以完全覆盖金属液表面为宜。步骤五中以5~20cm/s的速度均匀搅拌的作用是为了更有效的发挥熔炼剂对熔体的精炼效果。The usage amount of the smelting agent in step 2 and step 5 of this embodiment is 0.5%-0.8% of the weight of the molten metal, and it is advisable to completely cover the surface of the molten metal in step 2. The role of uniform stirring at a speed of 5-20 cm/s in step five is to more effectively exert the refining effect of the melting agent on the melt.
具体实施方式二:本实施方式与具体实施方式一不同的是步骤一中每块镁件的质量为0.25~2.0kg。其它步骤及参数与具体实施方式一相同。Embodiment 2: This embodiment differs from Embodiment 1 in that the mass of each magnesium piece in Step 1 is 0.25-2.0 kg. Other steps and parameters are the same as those in Embodiment 1.
具体实施方式三:本实施方式与具体实施方式二不同的是步骤一所述镁件的形状为矩形块状或饼状。其它步骤及参数与具体实施方式二相同。Embodiment 3: This embodiment is different from Embodiment 2 in that the shape of the magnesium piece in step 1 is a rectangular block or cake. Other steps and parameters are the same as in the second embodiment.
具体实施方式四:本实施方式与具体实施方式一至三之一不同的是步骤一热压的温度为150~350℃,热压的压力为120~300Mpa。其它步骤及参数与具体实施方式一至三之一相同。Embodiment 4: This embodiment differs from Embodiments 1 to 3 in that the temperature of hot pressing in step 1 is 150-350° C., and the pressure of hot pressing is 120-300 MPa. Other steps and parameters are the same as those in Embodiments 1 to 3.
具体实施方式五:本实施方式与具体实施方式一至四之一不同的是步骤二和步骤五中所述的熔炼剂按重量百分比由35%~41%的KCl,40%~46%的MgCl2,5%~8%的BaCl2,3%~5%的CaF2,NaCl+CaCl2≤6%和MgO≤1.5%组成。其它步骤及参数与具体实施方式一至四之一相同。Embodiment 5: The difference between this embodiment and Embodiment 1 to 4 is that the smelting agent described in step 2 and step 5 is composed of 35% to 41% KCl and 40% to 46% MgCl by weight percentage. , 5% to 8% of BaCl 2 , 3% to 5% of CaF 2 , NaCl+CaCl 2 ≤ 6% and MgO ≤ 1.5%. Other steps and parameters are the same as in one of the specific embodiments 1 to 4.
具体实施方式六:本实施方式与具体实施方式一至五之一不同的是步骤二和步骤五中所述的预热处理后的熔炼剂是在120~180℃温度下干燥至熔炼剂中H2O的质量含量在0.5%以下得到的。其它步骤及参数与具体实施方式一至五之一相同。Embodiment 6: The difference between this embodiment and one of Embodiments 1 to 5 is that the smelting agent after the preheating treatment described in Step 2 and Step 5 is dried at a temperature of 120-180°C to the H 2 in the smelting agent The mass content of O is obtained below 0.5%. Other steps and parameters are the same as one of the specific embodiments 1 to 5.
具体实施方式七:本实施方式与具体实施方式一至六之一不同的是步骤三采用钟罩压入式加入所需镁件质量的1/3~1/2,其中钟罩移动至与熔炼炉的炉底距离为100mm处。其它步骤及参数与具体实施方式一至六之一相同。Specific embodiment 7: The difference between this embodiment and one of the specific embodiments 1 to 6 is that step 3 adopts the bell jar to press-in to add 1/3 to 1/2 of the mass of the required magnesium parts, and the bell jar moves to the smelting furnace The furnace bottom distance is 100mm. Other steps and parameters are the same as one of the specific embodiments 1 to 6.
本实施方式采用钟罩压入式加入镁件,钟罩与炉底之间留有一定空间,钟罩在熔体中可以进行水平移动。In this embodiment, the bell jar is press-fitted to add magnesium parts, and there is a certain space between the bell jar and the bottom of the furnace, and the bell jar can move horizontally in the melt.
具体实施方式八:本实施方式与具体实施方式一至七之一不同的是步骤五采用钟罩压入式加入剩余的镁件,其中钟罩移动至与熔炼炉的炉底距离为100mm处。其它步骤及参数与具体实施方式一至七之一相同。Embodiment 8: The difference between this embodiment and one of Embodiments 1 to 7 is that step 5 uses a bell jar to press-in to add the remaining magnesium parts, wherein the bell jar moves to a distance of 100 mm from the furnace bottom of the melting furnace. Other steps and parameters are the same as one of the specific embodiments 1 to 7.
实施例一:本实施例采用AZ91镁合金屑制备铝镁中间合金AlMg10的方法按下列步骤实施:Embodiment one: the present embodiment adopts AZ91 magnesium alloy shavings to prepare the method for aluminum-magnesium master alloy AlMg10 to implement according to the following steps:
一、将生产加工中产生的镁合金废屑除油后烘干,然后把烘干的镁合金废屑通过压力机在热压温度300℃,热压压力为180Mpa的条件下热压制成每块1kg的镁件;1. Degreasing and drying the magnesium alloy waste generated during production and processing, and then hot pressing the dried magnesium alloy waste through a press at a hot pressing temperature of 300°C and a hot pressing pressure of 180Mpa to make each A 1kg piece of magnesium;
二、依照化学式AlMg10,按化学计量比称取铝锭条和镁件,沿着熔炼炉的炉壁排列铝锭条,开启熔炼炉熔化铝锭条,然后均匀撒上经预热处理后的熔炼剂,得到铝液;2. According to the chemical formula AlMg10, weigh the aluminum ingots and magnesium parts according to the stoichiometric ratio, arrange the aluminum ingots along the furnace wall of the melting furnace, turn on the melting furnace to melt the aluminum ingots, and then evenly sprinkle the preheated smelting agent to obtain liquid aluminum;
三、将铝液升温至760℃,采用钟罩压入式加入7kg的镁件,待镁件全部熔化后停炉,以5cm/s的速度搅拌3分钟,得到含镁的铝液;3. Raise the temperature of the molten aluminum to 760°C, add 7kg of magnesium parts by pressing in a bell jar, stop the furnace after all the magnesium parts are melted, and stir for 3 minutes at a speed of 5cm/s to obtain a molten aluminum containing magnesium;
四、将熔炼炉升温至760℃,采用钟罩压入式加入剩余的7kg镁件,待镁件全部熔化后停炉,以5cm/s的速度搅拌3分钟,得到铝镁液;4. Raise the temperature of the smelting furnace to 760°C, add the remaining 7kg of magnesium parts by pressing the bell jar, stop the furnace after all the magnesium parts are melted, and stir for 3 minutes at a speed of 5cm/s to obtain aluminum-magnesium liquid;
五、熔炼炉升温至740℃,在铝镁液表面均匀加入经预热处理后的熔炼剂对熔体进行精炼,同时以10cm/s的速度均匀搅拌,精炼时间为10分钟,静置5分钟后撇渣,得到熔融铝液;5. Heat up the melting furnace to 740°C, evenly add the preheated melting agent to the surface of the aluminum-magnesium liquid to refine the melt, and at the same time stir evenly at a speed of 10cm/s, the refining time is 10 minutes, and stand for 5 minutes Post skimming to obtain molten aluminum;
六、在步骤五的熔融铝液温度为730℃的条件下,利用旋转除气机使用N2与Cl2的混合气体进行除气处理,利用测氢仪测量氢含量,当氢含量达到0.2ml/100gAl以下时,停止除气静置15分钟后撇渣,然后再在熔融铝液温度为720℃时进行撇渣浇铸成锭,得到铝镁中间合金,完成含铝的镁合金废屑的回收利用。6. Under the condition that the molten aluminum temperature in step 5 is 730°C, use a rotary degasser to use a mixed gas of N 2 and Cl 2 for degassing treatment, and use a hydrogen detector to measure the hydrogen content. When the hydrogen content reaches 0.2ml /100gAl or less, stop degassing and let it stand for 15 minutes to skim off the slag, then skim off the slag and cast it into an ingot when the temperature of the molten aluminum is 720°C to obtain an aluminum-magnesium master alloy and complete the recovery of aluminum-containing magnesium alloy waste use.
本实施例Mg的回收率为90.31%,具体实验数据见下表1。The recovery rate of Mg in this embodiment is 90.31%, and the specific experimental data are shown in Table 1 below.
表1Table 1
实施例二:本实施例采用AZ31镁合金屑制备铝镁中间合金AlMg5的方法按下列步骤实施:Embodiment two: the method that present embodiment adopts AZ31 magnesium alloy shavings to prepare aluminum-magnesium master alloy AlMg5 is implemented according to the following steps:
一、将生产加工中产生的镁合金废屑除油后烘干,然后把烘干的镁合金废屑在压力机在热压温度200℃,热压压力为150Mpa的条件下热压制成每块1.5kg的镁件;1. Degreasing and drying the magnesium alloy waste generated during production and processing, and then hot pressing the dried magnesium alloy waste in a press at a hot pressing temperature of 200°C and a hot pressing pressure of 150Mpa to make each A 1.5kg piece of magnesium;
二、依照化学式AlMg5,按化学计量比称取铝锭条和镁件,沿着熔炼炉的炉壁排列铝锭条,开启熔炼炉熔化铝锭条,然后均匀撒上经预热处理后的熔炼剂,得到铝液;2. According to the chemical formula AlMg5, weigh the aluminum ingots and magnesium parts according to the stoichiometric ratio, arrange the aluminum ingots along the furnace wall of the melting furnace, turn on the melting furnace to melt the aluminum ingots, and then evenly sprinkle the preheated smelting agent to obtain liquid aluminum;
三、将铝液升温至740℃,采用钟罩压入式加入2kg的镁件,待镁件全部熔化后停炉,以10cm/s的速度搅拌3分钟,得到含镁的铝液;3. Raise the temperature of the molten aluminum to 740°C, add 2kg of magnesium parts by pressing in a bell jar, stop the furnace after all the magnesium parts are melted, and stir for 3 minutes at a speed of 10cm/s to obtain a molten aluminum containing magnesium;
四、将熔炼炉升温至740℃,采用钟罩压入式加入剩余的4kg镁件,待镁件全部熔化后停炉,以10cm/s的速度搅拌3分钟,得到铝镁液;4. Raise the temperature of the smelting furnace to 740°C, add the remaining 4kg of magnesium parts by pressing the bell jar, stop the furnace after all the magnesium parts are melted, and stir for 3 minutes at a speed of 10cm/s to obtain aluminum-magnesium liquid;
五、熔炼炉升温至740℃,在铝镁液表面均匀加入经预热处理后的熔炼剂对熔体进行精炼,同时以10cm/s的速度均匀搅拌,精炼时间为8分钟,静置10分钟后撇渣,得到熔融铝液;5. Heat up the melting furnace to 740°C, evenly add the preheated melting agent to the surface of the aluminum-magnesium liquid to refine the melt, and at the same time stir evenly at a speed of 10cm/s, the refining time is 8 minutes, and stand for 10 minutes Post skimming to obtain molten aluminum;
六、在步骤五的熔融铝液温度为730℃的条件下,利用旋转除气机使用N2与Cl2的混合气体进行除气处理,利用测氢仪测量氢含量,当氢含量达到0.2ml/100gAl以下时,停止除气静置10分钟后撇渣,然后再在熔融铝液温度为710℃时进行撇渣浇铸成锭,得到铝镁中间合金,完成含铝的镁合金废屑的回收利用。6. Under the condition that the molten aluminum temperature in step 5 is 730°C, use a rotary degasser to use a mixed gas of N 2 and Cl 2 for degassing treatment, and use a hydrogen detector to measure the hydrogen content. When the hydrogen content reaches 0.2ml /100gAl or less, stop degassing and let it stand for 10 minutes before skimming, then skimming and casting into ingots when the temperature of molten aluminum is 710°C, to obtain aluminum-magnesium master alloys, and complete the recovery of aluminum-containing magnesium alloy waste use.
本实施例Mg的回收率为92.32%,具体实验数据见下表2。The recovery rate of Mg in this embodiment is 92.32%, and the specific experimental data is shown in Table 2 below.
表2Table 2
实施例三:本实施例采用AZ61镁合金屑制备铝镁中间合金AlMg10的方法按下列步骤实施:Embodiment three: the present embodiment adopts AZ61 magnesium alloy shavings to prepare the method for aluminum-magnesium master alloy AlMg10 to implement according to the following steps:
一、将生产加工中产生的镁合金废屑除油后烘干,然后把烘干的镁合金废屑在压力机在热压温度250℃,热压压力为200Mpa的条件下热压制成每块0.5kg的镁件;1. Degreasing and drying the magnesium alloy waste generated during production and processing, and then hot-pressing the dried magnesium alloy waste in a press at a hot-pressing temperature of 250°C and a hot-pressing pressure of 200Mpa to make each A 0.5kg piece of magnesium;
二、依照化学式AlMg10,按化学计量比称取铝锭条和镁件,沿着熔炼炉的炉壁排列铝锭条,开启熔炼炉熔化铝锭条,然后均匀撒上经预热处理后的熔炼剂,得到铝液;2. According to the chemical formula AlMg10, weigh the aluminum ingots and magnesium parts according to the stoichiometric ratio, arrange the aluminum ingots along the furnace wall of the melting furnace, turn on the melting furnace to melt the aluminum ingots, and then evenly sprinkle the preheated smelting agent to obtain liquid aluminum;
三、将铝液升温至740℃,采用钟罩压入式加入6.5kg的镁件,待镁件全部熔化后停炉,以8cm/s的速度搅拌3分钟,得到含镁的铝液;3. Raise the temperature of the molten aluminum to 740°C, add 6.5kg of magnesium parts by pressing in a bell jar, stop the furnace after all the magnesium parts are melted, and stir for 3 minutes at a speed of 8cm/s to obtain a molten aluminum containing magnesium;
四、将熔炼炉升温至740℃,采用钟罩压入式加入剩余的6.5kg镁件,待镁件全部熔化后停炉,以8cm/s的速度搅拌3分钟,得到铝镁液;4. Raise the temperature of the smelting furnace to 740°C, add the remaining 6.5 kg of magnesium parts by pressing the bell jar, stop the furnace after all the magnesium parts are melted, and stir for 3 minutes at a speed of 8 cm/s to obtain aluminum-magnesium liquid;
五、熔炼炉升温至740℃,在铝镁液表面均匀加入经预热处理后的熔炼剂对熔体进行精炼,同时以5cm/s的速度均匀搅拌,精炼时间为8分钟,静置10分钟后撇渣,得到熔融铝液;5. Heat up the melting furnace to 740°C, evenly add the preheated melting agent to the surface of the aluminum-magnesium liquid to refine the melt, and at the same time stir evenly at a speed of 5cm/s, the refining time is 8 minutes, and stand for 10 minutes Post skimming to obtain molten aluminum;
六、在步骤五的熔融铝液温度为720℃的条件下,利用旋转除气机使用N2与Cl2的混合气体进行除气处理,利用测氢仪测量氢含量,当氢含量达到0.2ml/100gAl以下时,停止除气静置10分钟后撇渣,然后再在熔融铝液温度为700℃时进行撇渣浇铸成锭,得到铝镁中间合金,完成含铝的镁合金废屑的回收利用。6. Under the condition that the molten aluminum temperature in step 5 is 720°C, use a rotary degasser to use a mixed gas of N 2 and Cl 2 for degassing treatment, and use a hydrogen detector to measure the hydrogen content. When the hydrogen content reaches 0.2ml /100gAl or less, stop degassing and let it stand for 10 minutes before skimming, and then skimming and casting into ingots when the temperature of molten aluminum is 700°C, to obtain aluminum-magnesium master alloys, and complete the recovery of aluminum-containing magnesium alloy waste use.
本实施例Mg的回收率为90.70%,具体实验数据见下表3。The recovery rate of Mg in this embodiment is 90.70%, and the specific experimental data is shown in Table 3 below.
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