CN116240416A - Low-foam low-smoke refining agent for rare earth magnesium alloy and preparation method thereof - Google Patents
Low-foam low-smoke refining agent for rare earth magnesium alloy and preparation method thereof Download PDFInfo
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- 238000007670 refining Methods 0.000 title claims abstract description 96
- 239000003795 chemical substances by application Substances 0.000 title claims abstract description 76
- 229910052761 rare earth metal Inorganic materials 0.000 title claims abstract description 55
- 229910000861 Mg alloy Inorganic materials 0.000 title claims abstract description 54
- 150000002910 rare earth metals Chemical class 0.000 title claims abstract description 52
- 239000000779 smoke Substances 0.000 title claims abstract description 27
- 238000002360 preparation method Methods 0.000 title claims abstract description 11
- 239000006260 foam Substances 0.000 title claims abstract 6
- 150000003839 salts Chemical class 0.000 claims abstract description 45
- 230000004907 flux Effects 0.000 claims abstract description 39
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 30
- 238000000034 method Methods 0.000 claims abstract description 27
- 238000003756 stirring Methods 0.000 claims abstract description 21
- 229910004261 CaF 2 Inorganic materials 0.000 claims abstract description 16
- 238000010438 heat treatment Methods 0.000 claims abstract description 15
- 239000011780 sodium chloride Substances 0.000 claims abstract description 15
- 229910016036 BaF 2 Inorganic materials 0.000 claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 238000007873 sieving Methods 0.000 claims abstract description 8
- 238000003723 Smelting Methods 0.000 claims abstract description 6
- 238000001816 cooling Methods 0.000 claims abstract description 5
- 238000002156 mixing Methods 0.000 claims abstract description 5
- 238000005187 foaming Methods 0.000 claims description 21
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 229910002804 graphite Inorganic materials 0.000 claims description 6
- 239000010439 graphite Substances 0.000 claims description 6
- 238000000227 grinding Methods 0.000 claims description 6
- 239000002994 raw material Substances 0.000 claims description 6
- 229910001018 Cast iron Inorganic materials 0.000 claims description 3
- 229910052693 Europium Inorganic materials 0.000 claims description 3
- 229910052688 Gadolinium Inorganic materials 0.000 claims description 3
- 229910052593 corundum Inorganic materials 0.000 claims description 3
- 239000010431 corundum Substances 0.000 claims description 3
- 238000010907 mechanical stirring Methods 0.000 claims description 3
- 229910052727 yttrium Inorganic materials 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 2
- 230000008569 process Effects 0.000 abstract description 15
- 230000000694 effects Effects 0.000 abstract description 9
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 abstract description 5
- 230000005484 gravity Effects 0.000 abstract description 5
- 230000002829 reductive effect Effects 0.000 abstract description 4
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 abstract description 2
- 229910017053 inorganic salt Inorganic materials 0.000 abstract description 2
- 238000007711 solidification Methods 0.000 abstract description 2
- 230000008023 solidification Effects 0.000 abstract description 2
- 229910045601 alloy Inorganic materials 0.000 description 12
- 239000000956 alloy Substances 0.000 description 12
- 239000000155 melt Substances 0.000 description 11
- 239000000203 mixture Substances 0.000 description 10
- 238000002844 melting Methods 0.000 description 9
- 230000008018 melting Effects 0.000 description 9
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 8
- 239000007789 gas Substances 0.000 description 8
- 229910052749 magnesium Inorganic materials 0.000 description 8
- 239000011777 magnesium Substances 0.000 description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 238000005266 casting Methods 0.000 description 5
- 239000000460 chlorine Substances 0.000 description 5
- 150000003841 chloride salts Chemical class 0.000 description 3
- 150000001805 chlorine compounds Chemical class 0.000 description 3
- 150000004673 fluoride salts Chemical class 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 229910052684 Cerium Inorganic materials 0.000 description 2
- 229910052692 Dysprosium Inorganic materials 0.000 description 2
- 229910052689 Holmium Inorganic materials 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 229910052779 Neodymium Inorganic materials 0.000 description 2
- 229910052772 Samarium Inorganic materials 0.000 description 2
- 229910052769 Ytterbium Inorganic materials 0.000 description 2
- 230000032683 aging Effects 0.000 description 2
- 150000001804 chlorine Chemical class 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 150000002221 fluorine Chemical class 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 229910052746 lanthanum Inorganic materials 0.000 description 2
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 description 2
- 238000010128 melt processing Methods 0.000 description 2
- 239000007769 metal material Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- -1 KCl Chemical class 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000013016 damping Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229910052588 hydroxylapatite Inorganic materials 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 150000008040 ionic compounds Chemical class 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 229910052919 magnesium silicate Inorganic materials 0.000 description 1
- 235000019792 magnesium silicate Nutrition 0.000 description 1
- 239000000391 magnesium silicate Substances 0.000 description 1
- ZADYMNAVLSWLEQ-UHFFFAOYSA-N magnesium;oxygen(2-);silicon(4+) Chemical compound [O-2].[O-2].[O-2].[Mg+2].[Si+4] ZADYMNAVLSWLEQ-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- XYJRXVWERLGGKC-UHFFFAOYSA-D pentacalcium;hydroxide;triphosphate Chemical compound [OH-].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O XYJRXVWERLGGKC-UHFFFAOYSA-D 0.000 description 1
- 230000008654 plant damage Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000006104 solid solution Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C1/00—Making non-ferrous alloys
- C22C1/06—Making non-ferrous alloys with the use of special agents for refining or deoxidising
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C23/00—Alloys based on magnesium
- C22C23/06—Alloys based on magnesium with a rare earth metal as the next major constituent
-
- 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
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
技术领域technical field
本发明属于金属材料及冶金技术领域,特别涉及稀土镁合金用低泡少烟精炼剂及其制备方法。The invention belongs to the technical field of metal materials and metallurgy, and in particular relates to a low-foaming and less-smoke refining agent for rare earth magnesium alloys and a preparation method thereof.
背景技术Background technique
镁合金比强度高、比刚度高、阻尼性能优异,作为金属材料兼具耐真空、耐辐照、耐原子氧等特性,在航空航天、交通运输、3C数码等领域有着广阔的应用前景。稀土镁合金是镁合金的重要组成部分,该类合金将稀土作为主加元素,利用稀土元素在镁合金中固溶度大、引起晶格畸变强烈、时效过程中形成弥散析出相的特性,起到优异的固溶、时效强化效果,突破了镁合金绝对强韧性不足的瓶颈。稀土元素还能在镁合金凝固过程中富集在溶质界面前沿引起成分过冷,细化合金晶粒,进一步提升镁合金的抗蠕变性能及室高温强度。目前,以VW63Z、WE43B为代表的稀土镁合金,已在舱体、机匣等航空航天产品上取得广泛应用。Magnesium alloy has high specific strength, high specific stiffness, and excellent damping performance. As a metal material, it has the characteristics of vacuum resistance, radiation resistance, and atomic oxygen resistance. It has broad application prospects in aerospace, transportation, 3C digital and other fields. Rare earth magnesium alloy is an important part of magnesium alloy. This type of alloy uses rare earth as the main addition element, and utilizes the characteristics of large solid solubility of rare earth elements in magnesium alloys, causing strong lattice distortion, and forming dispersed precipitates during aging. It has achieved excellent solid solution and aging strengthening effects, breaking through the bottleneck of insufficient absolute strength and toughness of magnesium alloys. Rare earth elements can also be enriched at the front of the solute interface during the solidification process of the magnesium alloy to cause supercooling of the composition, refine the alloy grains, and further improve the creep resistance and room temperature strength of the magnesium alloy. At present, rare earth magnesium alloys represented by VW63Z and WE43B have been widely used in aerospace products such as cabins and receivers.
但镁和稀土化学性质十分活泼,高温下熔体表面生成的表面膜P-B比小于1,无法对熔体起到充分的保护作用,不仅会导致镁合金当中产生大量的夹杂物,还会在熔炼过程中引起剧烈的燃烧,严重影响生产的安全性。向合金熔体内填加熔剂是实际生产中最常用的保护手段,成本低廉、操作简便、除杂效率高。熔剂可以细分为覆盖剂和精炼剂:覆盖剂在镁熔体表面形成完整连续的覆盖层,从而抑制镁熔体的氧化、燃烧,减少熔炼过程中夹杂物的生成;精炼剂在镁合金精炼过程中加入,利用精炼剂对夹杂物的润湿、捕捉能力要优于镁熔体的特性,使夹杂物自发地向熔剂迁移、吸附、聚集、沉降,实现夹杂物的去除。精炼效果的好坏,会直接影响镁合金产品的质量。However, the chemical properties of magnesium and rare earth are very active. The P-B ratio of the surface film formed on the surface of the melt at high temperature is less than 1, which cannot fully protect the melt. In the process, violent combustion is caused, which seriously affects the safety of production. Filling the alloy melt with flux is the most commonly used protection method in actual production, with low cost, easy operation and high efficiency of impurity removal. Flux can be subdivided into covering agent and refining agent: covering agent forms a complete and continuous covering layer on the surface of magnesium melt, thereby inhibiting the oxidation and combustion of magnesium melt, and reducing the formation of inclusions during smelting; refining agent is used in magnesium alloy refining Adding in the process, using the refining agent to wet and capture the inclusions is better than the characteristics of the magnesium melt, so that the inclusions spontaneously migrate, adsorb, aggregate, and settle to the flux to achieve the removal of the inclusions. The quality of refining effect will directly affect the quality of magnesium alloy products.
传统镁合金多采用RJ2熔剂进行精炼,但稀土镁合金熔体密度大,RJ2熔剂难以在熔体内充分沉降,易在铸件中产生熔剂夹杂。目前稀土镁合金多采用JDMJ或RJ6进行精炼。JDMJ对于ZM6等低稀土含量的稀土镁合金,净化效果较好,但MgCl2会与稀土发生如下反应3MgCl2+2[RE]→2RECl3+3Mg,导致稀土原子损耗,因此对于VW63Z等高稀土含量的稀土镁合金,优选的精炼剂是RJ6熔剂。RJ6熔剂的主要成分为Ca、K、Ba的氯盐,具体质量分数为:54~56%KCl,27~29%CaCl2,14~16%BaCl2,0~5%CaF2。氯盐的熔点较低,撒入镁合金熔体中会迅速液化,在熔炼过程中会生成HCl、Cl2等气体,RJ6组元中氯盐比例过高,产生的腐蚀性气体对操作人员身体健康有不利影响,使铸造设备和熔炼厂房产生严重的腐蚀,也不利于环境的保护。此外,RJ6的密度也较低,Traditional magnesium alloys mostly use RJ2 flux for refining, but the rare earth magnesium alloy melt has a high density, and it is difficult for RJ2 flux to fully settle in the melt, and it is easy to produce flux inclusions in castings. At present, rare earth magnesium alloys are mostly refined by JDMJ or RJ6. JDMJ has a good purification effect for rare earth magnesium alloys with low rare earth content such as ZM6, but MgCl 2 will react with rare earth as follows: 3MgCl 2 +2[RE]→2RECl 3 +3Mg, resulting in the loss of rare earth atoms, so for VW63Z and other high rare earth content of rare earth magnesium alloy, the preferred refining agent is RJ6 flux. The main components of RJ6 flux are chloride salts of Ca, K and Ba, and the specific mass fractions are: 54-56% KCl, 27-29% CaCl 2 , 14-16% BaCl 2 , 0-5% CaF 2 . The melting point of chlorine salt is low, and it will be liquefied rapidly when sprinkled into the magnesium alloy melt. During the smelting process, HCl, Cl 2 and other gases will be generated. The proportion of chlorine salt in the RJ6 component is too high, and the corrosive gas produced will be harmful to the operator's body. It has adverse effects on health, causes serious corrosion of foundry equipment and smelting workshops, and is not conducive to environmental protection. In addition, the density of RJ6 is also low,
针对上述现状,专利CN103468976A制备了一种在MgCl2、CaCl2、BaCl2、NaCl和CaF2中加入5~10%MgF2的覆盖剂和精炼剂,能够有效减少熔体夹杂,减少有害气体的产生。但该熔剂依旧含有MgCl2,不适用于稀土镁合金。专利CN105349816A制备了含有BaCO3、CaSO4、LiCl、羟基磷灰石和硅酸镁的覆盖用熔剂,减少了氯化物的含量,利用碳酸盐等发泡物质受热分解释放无公害气体,覆盖在熔体表面,起到保护熔体的作用。但该熔剂不适用于镁合金的精炼。In view of the above situation, the patent CN103468976A has prepared a covering agent and refining agent that adds 5-10% MgF 2 to MgCl 2 , CaCl 2 , BaCl 2 , NaCl and CaF 2 , which can effectively reduce melt inclusions and reduce harmful gases. produce. But the flux still contains MgCl 2 , which is not suitable for rare earth magnesium alloys. Patent CN105349816A prepares a covering flux containing BaCO 3 , CaSO 4 , LiCl, hydroxyapatite and magnesium silicate, which reduces the content of chlorides, uses foaming materials such as carbonates to decompose by heat to release pollution-free gases, and covers the The melt surface plays a role in protecting the melt. But this flux is not suitable for the refining of magnesium alloy.
发明内容Contents of the invention
为了克服上述缺陷,本发明提供了一种稀土镁合金用低泡少烟精炼剂,其特征在于,包括下述质量百分比的组分:In order to overcome the above defects, the present invention provides a low-foaming and less-smoke refining agent for rare earth magnesium alloy, which is characterized in that it comprises the following components in mass percentage:
本发明还提供了一种稀土镁合金用低泡少烟精炼剂的制备方法,其特征在于,包括下述步骤:The present invention also provides a preparation method of a low-foaming and less-smoke refining agent for rare earth magnesium alloy, which is characterized in that it comprises the following steps:
S1配料:将CaCl2、BaCl2、NaCl、CaF2、BaF2、KF和KCl按配比混合均匀后得到混合盐;S1 ingredients: mix CaCl 2 , BaCl 2 , NaCl, CaF 2 , BaF 2 , KF and KCl uniformly according to the proportion to obtain mixed salt;
S2熔炼:将坩埚加热至100℃~150℃,将混合盐加入坩埚中,将坩埚升温至800℃~850℃,升温过程中搅拌混合盐,直至混合盐完全熔化;S2 Melting: Heat the crucible to 100°C-150°C, add the mixed salt into the crucible, raise the temperature of the crucible to 800°C-850°C, stir the mixed salt during the heating process until the mixed salt is completely melted;
S3浇注:将液态混合盐充分搅拌后,浇注到模具中,凝固冷却后得到块状熔剂;S3 pouring: After fully stirring the liquid mixed salt, pour it into the mold, solidify and cool to obtain a block flux;
S4破碎过筛:将块状熔剂破碎,碾磨得到粉状熔剂,过筛后得到精炼剂。S4 crushing and sieving: crush the bulk flux, grind it to obtain powdery flux, and obtain refining agent after sieving.
进一步的是,所述步骤S1中加入的原料配比为按质量百分比计:Further, the ratio of raw materials added in the step S1 is by mass percentage:
进一步的是,所述步骤S1中,CaCl2、BaCl2、NaCl、CaF2、BaF2、KF和KCl在按配比混合前在220℃~250℃条件下烘干脱水。Further, in the step S1, CaCl 2 , BaCl 2 , NaCl, CaF 2 , BaF 2 , KF and KCl are dried and dehydrated at 220° C. to 250° C. before mixing according to the proportion.
进一步的是,所述步骤S1中,将所得混合盐置于干燥密闭容器内或者封入普通密闭容器并存放于相对湿度低的环境中。Further, in the step S1, the obtained mixed salt is placed in a dry airtight container or sealed in an ordinary airtight container and stored in an environment with low relative humidity.
进一步的是,所述稀土镁合金中稀土元素包括选自Gd,Y,Nd,La,Ce,Sm,Sc,Er,Dy,Ho,Yb或Eu中的一种或一种以上的组合,稀土原子总质量百分比为≥6%。Further, the rare earth element in the rare earth magnesium alloy includes one or more combinations selected from Gd, Y, Nd, La, Ce, Sm, Sc, Er, Dy, Ho, Yb or Eu, and the rare earth The total atomic mass percentage is ≥6%.
进一步的是,所述步骤S2中,坩埚材质为石墨、刚玉、或者铸铁,搅拌方式为浇勺机械搅拌。Further, in the step S2, the material of the crucible is graphite, corundum, or cast iron, and the stirring method is mechanical stirring with a ladle.
进一步的是,所述步骤S2中,在将混合盐加入坩埚中后,坩埚升温速率为200℃/h~400℃/h。Further, in the step S2, after adding the mixed salt into the crucible, the heating rate of the crucible is 200°C/h-400°C/h.
进一步的是,所述步骤S3中,模具材质为石墨。Further, in the step S3, the material of the mold is graphite.
进一步的是,所述步骤S4中,过筛的筛子目数为10目~20目。Further, in the step S4, the mesh size of the sieve is 10 mesh to 20 mesh.
本发明调整无机盐配比,使用氟化物替代部分氯化物,适当增大比重剂的含量,可在保证精炼剂精炼效果的基础上,有效减少精炼过程中腐蚀性烟气的释放,减轻对人员、设备、厂房的损害。The invention adjusts the ratio of inorganic salts, uses fluoride to replace part of chloride, and appropriately increases the content of specific gravity agent, which can effectively reduce the release of corrosive fumes during the refining process on the basis of ensuring the refining effect of the refining agent, and reduce the impact on personnel. , equipment, plant damage.
附图说明Description of drawings
图1为采用本发明方法的实施例1中浇注后得到的块状熔剂的外观图;Fig. 1 is the exterior view of the block flux that obtains after pouring in the embodiment 1 that adopts the inventive method;
图2为采用本发明方法的实施例1中得到的精炼剂A的冷却曲线。Fig. 2 is a cooling curve of refining agent A obtained in Example 1 using the method of the present invention.
具体实施方式Detailed ways
下面通过对本发明进行详细说明,本发明的特点和优点将随着这些说明而变得更为清楚、明确。The following describes the present invention in detail, and the features and advantages of the present invention will become more clear and definite along with these descriptions.
在这里专用的词“示例性”意为“用作例子、实施例或说明性”。这里作为“示例性”所说明的任何实施例不必解释为优于或好于其它实施例。尽管在附图中示出了实施例的各种方面,但是除非特别指出,不必按比例绘制附图。The word "exemplary" is used exclusively herein to mean "serving as an example, embodiment, or illustration." Any embodiment described herein as "exemplary" is not necessarily to be construed as superior or better than other embodiments. While various aspects of the embodiments are shown in drawings, the drawings are not necessarily drawn to scale unless specifically indicated.
本发明精炼剂针对稀土镁合金传统精炼剂氯盐含量高、精炼过程中易释放腐蚀性气体的问题,在保证不含MgCl2等镁盐、防止因精炼剂造成稀土元素损耗的基础上,调整无机盐成分的种类与含量,减少精炼剂中氯化物的比重,增加对应阳离子的氟盐,适当提升了熔剂的熔点,减缓了精炼过程中精炼剂的熔化速率,减少了精炼过程中HCl、Cl2等有害气体的释放。The refining agent of the present invention aims at the problem that the traditional refining agent of rare earth magnesium alloy has high chloride salt content and easy release of corrosive gas during the refining process. The type and content of inorganic salt components reduce the proportion of chloride in the refining agent and increase the fluoride salt corresponding to the cation, which appropriately increases the melting point of the flux, slows down the melting rate of the refining agent during the refining process, and reduces the amount of HCl and Cl in the refining process. 2 release of harmful gases.
优化后的精炼剂成分具有良好的造渣能力和精炼能力,由于氟盐含量较多,精炼剂密度较大,提升了精炼剂在熔体内的沉降速率,保证精炼剂-夹杂聚合物能在较短时间完成沉降,减小了熔剂夹杂的可能性,缩短了熔体处理的时间。尤其适合于熔体粘度高、密度大的稀土含量镁合金的精炼处理。The optimized refining agent composition has good slagging ability and refining ability. Due to the high content of fluorine salts, the refining agent has a higher density, which improves the settling rate of the refining agent in the melt and ensures that the refining agent-inclusion polymer can Settling is completed in a short time, which reduces the possibility of flux inclusions and shortens the time for melt processing. It is especially suitable for the refining treatment of rare earth content magnesium alloys with high melt viscosity and high density.
本发明精炼剂的组分包括CaCl2、BaCl2、NaCl、CaF2、BaF2、KF和KCl。The components of the refining agent of the present invention include CaCl 2 , BaCl 2 , NaCl, CaF 2 , BaF 2 , KF and KCl.
针对稀土镁合金传统精炼剂氯盐含量高、精炼过程中易释放腐蚀性气体的问题,本发明提出一种稀土镁合金用低泡少烟精炼剂,所包含的组分质量百分比范围为:CaCl2:20~36%;BaCl2:5~15%;NaCl:0~3%;CaF2:0.5~5%;BaF2:0~8%;KF:0.5~20%;KCl:余量。组分纯度是工业纯及以上的纯度。Aiming at the problem that the traditional refining agent of rare earth magnesium alloy has high content of chloride salt and easy release of corrosive gas during the refining process, the present invention proposes a low-foaming and less-smoke refining agent for rare earth magnesium alloy. The mass percentage range of the components contained is: CaCl 2 : 20-36%; BaCl 2 : 5-15%; NaCl: 0-3%; CaF 2 : 0.5-5%; BaF 2 : 0-8%; KF: 0.5-20%; The purity of components is technical purity and above.
本发明精炼剂可用于稀土镁合金熔炼过程中去除杂质元素与非金属夹杂物的精炼处理,具有精炼效果好、精炼过程产生腐蚀性烟气少、对人员设备和环境污染小的优点,能在较短静置时间内实现稀土镁合金的精炼处理,可有效应用于工业生产。所述稀土镁合金加入的稀土元素包括选自Gd,Y,Nd,La,Ce,Sm,Sc,Er,Dy,Ho,Yb或Eu中的一种或一种以上组合,稀土原子总质量百分比为≥6%。The refining agent of the present invention can be used in the refining treatment of removing impurity elements and non-metallic inclusions in the smelting process of rare earth magnesium alloy, and has the advantages of good refining effect, less corrosive fume generated in the refining process, and less pollution to personnel, equipment and the environment, and can be used in The refining treatment of the rare earth magnesium alloy can be realized within a short standing time, and can be effectively applied to industrial production. The rare earth elements added to the rare earth magnesium alloy include one or more combinations selected from Gd, Y, Nd, La, Ce, Sm, Sc, Er, Dy, Ho, Yb or Eu, and the total mass percentage of rare earth atoms is is ≥6%.
本发明适用于稀土镁合金的精炼处理。The invention is suitable for refining treatment of rare earth magnesium alloy.
本发明还提供了上述精炼剂的制备方法。The present invention also provides a preparation method of the above-mentioned refining agent.
上述一种稀土镁合金用低泡少烟精炼剂的制备方法包括以下步骤:The preparation method of the above-mentioned low-foaming and less-smoke refining agent for a rare earth magnesium alloy comprises the following steps:
S1配料:将CaCl2、BaCl2、NaCl、CaF2、KF和KCl按配比混合均匀后得到混合盐,置于干燥密闭容器内;该步骤中,干燥密闭容器可以是干燥皿、封口的塑料瓶,也可以封入普通密闭容器并存放于相对湿度低的环境中。该步骤中,加入的原料配比按所包含的组分质量百分比范围为:CaCl2:20~36%;BaCl2:5~15%;NaCl:0.5~3%;CaF2:1~5%;BaF2:2~8%;KF:5~20%;KCl:余量。该步骤中,CaCl2、BaCl2、NaCl、CaF2、BaF2、KF和KCl在配比前应在220℃~250℃条件下烘干脱水。S1 ingredients: mix CaCl 2 , BaCl 2 , NaCl, CaF 2 , KF and KCl according to the ratio to obtain mixed salt, and place it in a dry airtight container; in this step, the dry airtight container can be a drying dish or a sealed plastic bottle , and can also be sealed in ordinary airtight containers and stored in an environment with low relative humidity. In this step, the ratio of raw materials added is in the following ranges according to the mass percentage of the components: CaCl 2 : 20-36%; BaCl 2 : 5-15%; NaCl: 0.5-3%; CaF 2 : 1-5% ; BaF 2 : 2-8%; KF: 5-20%; KCl: balance. In this step, CaCl 2 , BaCl 2 , NaCl, CaF 2 , BaF 2 , KF and KCl should be dried and dehydrated at 220°C to 250°C before proportioning.
S2熔炼:将坩埚加热至100℃~150℃,将混合盐加入坩埚中,将坩埚升温至800℃~850℃,升温过程中用浇勺搅拌混合盐,直至混合盐完全熔化;该步骤中,坩埚材质优选是石墨,也可以是刚玉、铸铁,只需要耐温水平可达900℃;该步骤中,在将混合盐加入坩埚中后,坩埚升温速率优选是200℃/h~400℃/h,过快的升温速度存在爆沸的风险,过慢的升温速率影响了生产效率,且升温过程中可能存在熔盐的挥发;该步骤中,搅拌方式为机械搅拌,浇勺的材质没有指定,只需要保证不与熔盐反应,且能够耐受熔盐的高温。S2 Melting: Heat the crucible to 100°C-150°C, add the mixed salt into the crucible, raise the temperature of the crucible to 800°C-850°C, stir the mixed salt with a ladle during the heating process until the mixed salt is completely melted; in this step, The material of the crucible is preferably graphite, or corundum or cast iron, as long as the temperature resistance level can reach 900°C; in this step, after the mixed salt is added to the crucible, the heating rate of the crucible is preferably 200°C/h~400°C/h , there is a risk of bumping if the heating rate is too fast, and the production efficiency is affected by a too slow heating rate, and there may be volatilization of molten salt during the heating process; in this step, the stirring method is mechanical stirring, and the material of the ladle is not specified. It only needs to ensure that it does not react with the molten salt and can withstand the high temperature of the molten salt.
S3浇注:将液态混合盐充分搅拌后,浇注到模具中,凝固冷却后得到块状熔剂。该步骤中,模具材质优选为石墨。S3 Pouring: After the liquid mixed salt is fully stirred, it is poured into the mold, solidified and cooled to obtain a block flux. In this step, the mold material is preferably graphite.
S4破碎过筛:将块状熔剂破碎,置入研磨钵捣碎、碾磨,得到粉状熔剂,过筛后得到精炼剂,放于干燥密闭容器备用。该步骤中,筛子目数优选是10目~20目,但也可以低于10目或高于20目,过细的筛孔导致熔剂过筛效率低下,过粗的筛孔导致。S4 Crushing and sieving: crush the bulk flux, put it into a grinding bowl to crush, and grind to obtain a powdery flux, which is sieved to obtain a refining agent, which is stored in a dry airtight container for later use. In this step, the mesh size of the sieve is preferably 10 mesh to 20 mesh, but it can also be lower than 10 mesh or higher than 20 mesh. Too fine a mesh will result in low efficiency of flux sieving, and too coarse a mesh will cause flux.
本发明获得了下述技术效果:The present invention has obtained following technical effect:
(1)本发明稀土镁合金用低泡少烟精炼剂中,不含MgCl2,不会造成稀土元素的损耗;(1) The low-foaming and less-smoke refining agent for rare earth magnesium alloys of the present invention does not contain MgCl 2 , which will not cause loss of rare earth elements;
(2)本发明稀土镁合金用低泡少烟精炼剂中,减少了KCl、CaCl2、BaCl2等氯化物的比重,增加了KF、CaF、BaF2等氟盐,由于氟离子的电负性大于氯离子,离子半径更小,离子化合物间极性更强,因此制得的精炼剂熔点更高,撒入镁熔体后熔化减缓,降低了精炼剂与熔体作用的强烈程度。氯离子绝对含量也有所降低,[Cl]的活度下降,减少了2[Cl]→Cl2↑的反应的倾向,从而减少了精炼过程中腐蚀性有害气体的释放;(2) In the low-foaming and less-smoke refining agent for rare earth magnesium alloys of the present invention, the specific gravity of chlorides such as KCl, CaCl 2 , and BaCl 2 has been reduced, and fluorine salts such as KF, CaF, and BaF 2 have been increased. The polarity is greater than that of chloride ion, the ionic radius is smaller, and the polarity between the ionic compounds is stronger, so the melting point of the obtained refining agent is higher, and the melting is slowed down after being sprinkled into the magnesium melt, which reduces the intensity of the interaction between the refining agent and the melt. The absolute content of chloride ions is also reduced, and the activity of [Cl] decreases, which reduces the tendency of the reaction of 2[Cl]→Cl 2 ↑, thereby reducing the release of corrosive and harmful gases during the refining process;
(3)本发明稀土镁合金用低泡少烟精炼剂中,优化了无机盐中氯化物和氟化物的种类与含量,在保证良好的造渣能力与精炼能力的基础上,由于密度较大的氟盐质量分数较高,精炼剂的密度有所提升,精炼剂与熔体的分离性上升,减小了熔剂夹杂的可能性,能够在较短时间内完成夹杂的吸附、沉降和分离,缩短了熔体处理的时间。尤其适合于熔体粘度高、密度大的稀土含量镁合金的精炼处理。(3) In the low-foaming and less-smoke refining agent for rare earth magnesium alloys of the present invention, the types and contents of chlorides and fluorides in inorganic salts are optimized. On the basis of ensuring good slagging ability and refining ability, due to the high density The higher the mass fraction of fluoride salts, the higher the density of the refining agent, the higher the separation between the refining agent and the melt, reducing the possibility of flux inclusions, and the adsorption, sedimentation and separation of inclusions can be completed in a short period of time. The time for melt processing is shortened. It is especially suitable for the refining treatment of rare earth content magnesium alloys with high melt viscosity and high density.
实施例1Example 1
按下述步骤制备一种稀土镁合金用低泡少烟精炼剂,其组分和质量分数为:CaCl2:27%;BaCl2:5%;NaCl:1%;CaF2:5%;BaF2:8%;KF:18%;KCl:36%。Prepare a low-foaming and less-smoke refining agent for rare earth magnesium alloys according to the following steps, its components and mass fractions are: CaCl 2 : 27%; BaCl 2 : 5%; NaCl: 1%; CaF 2 : 5%; BaF 2 : 8%; KF: 18%; KCl: 36%.
本实施例的稀土镁合金用低泡少烟精炼剂制备步骤为:将上述原料按上述配比混合均匀后得到混合盐,置于干燥密闭容器内;将坩埚加热至120℃,将混合盐加入坩埚中,将坩埚升温至810℃,升温过程中用浇勺搅拌混合盐,直至混合盐完全熔化;将液态混合盐充分搅拌后,浇注到模具中,凝固冷却后得到块状熔剂(见图1),将块状熔剂破碎,置入研磨钵捣碎、碾磨,得到粉状熔剂,用筛孔目数为10目的筛子过筛后,得到精炼剂A放于干燥密闭容器备用。The preparation steps of the low-foaming and less-smoke refining agent for rare earth magnesium alloys in this example are as follows: mix the above-mentioned raw materials according to the above-mentioned ratio to obtain a mixed salt, and place it in a dry airtight container; heat the crucible to 120°C, add the mixed salt In the crucible, raise the temperature of the crucible to 810°C, and stir the mixed salt with a pouring spoon during the heating process until the mixed salt is completely melted; after fully stirring the liquid mixed salt, pour it into the mold, solidify and cool to obtain a block flux (see Figure 1 ), breaking the lumpy flux, putting it into a grinding bowl, crushing, and grinding to obtain a powdery flux, which is sieved through a sieve with a mesh number of 10 to obtain refining agent A and put in a dry airtight container for subsequent use.
图1为采用本发明方法的实施例1中浇注后得到的块状熔剂的外观图。块状溶剂外观如图1所示。图2为采用本发明方法的实施例1中得到的精炼剂A的冷却曲线。图2示出了对精炼剂A测量熔点得到的熔剂冷却曲线,如图2所示,从中测得熔点为约670℃。Fig. 1 is the exterior view of the block flux obtained after pouring in Example 1 using the method of the present invention. The appearance of block solvent is shown in Figure 1. Fig. 2 is a cooling curve of refining agent A obtained in Example 1 using the method of the present invention. Fig. 2 shows a flux cooling curve obtained by measuring the melting point of refining agent A, as shown in Fig. 2, from which the melting point was measured to be about 670°C.
在使用上述得到的精炼剂A时,在刷有涂料的铁质坩埚中撒入覆盖剂,加入纯镁并升温至780℃,期间撒入覆盖剂阻燃,随后加入中间合金至熔体成分配比为Mg-4Y-2Nd-1Gd,搅拌至中间合金充分熔化;精炼时,一边搅拌合金液,一边加入1.5wt.%上述精炼剂,精炼时间为10分钟;精炼处理完毕后捞渣、静置20min后重力浇注金属型试样,T6抗拉强度255MPa,延伸率2.2%。When using the refining agent A obtained above, sprinkle the covering agent in the painted iron crucible, add pure magnesium and raise the temperature to 780°C, during which the covering agent is sprinkled to prevent flames, and then add the master alloy to the melt composition distribution The ratio is Mg-4Y-2Nd-1Gd, stirring until the intermediate alloy is fully melted; during refining, while stirring the alloy liquid, add 1.5wt.% of the above refining agent, and the refining time is 10 minutes; after the refining process, remove the slag and let it stand After 20 minutes, gravity cast the metal sample, the T6 tensile strength is 255MPa, and the elongation is 2.2%.
实施例2Example 2
按下述步骤制备一种稀土镁合金用低泡少烟精炼剂,其组分和质量分数为:CaCl2:30%;BaCl2:10%;NaCl:2%;CaF2:4%;BaF2:6%;KF:16%;KCl:32%。Prepare a low-foaming and less-smoke refining agent for rare earth magnesium alloys according to the following steps, its components and mass fractions are: CaCl 2 : 30%; BaCl 2 : 10%; NaCl: 2%; CaF 2 : 4%; BaF 2 : 6%; KF: 16%; KCl: 32%.
本实施例的稀土镁合金用低泡少烟精炼剂制备步骤为:将上述原料按上述配比混合均匀后得到混合盐,置于干燥密闭容器内;将坩埚加热至130℃,将混合盐加入坩埚中,将坩埚升温至825℃,升温过程中用浇勺搅拌混合盐,直至混合盐完全熔化;将液态混合盐充分搅拌后,浇注到模具中,凝固冷却后得到块状熔剂;将块状熔剂破碎,置入研磨钵捣碎、碾磨,得到粉状熔剂,用筛孔目数为10目的筛子过筛后,得到精炼剂B放于干燥密闭容器备用。The preparation steps of the low-foaming and less-smoke refining agent for rare earth magnesium alloys in this example are as follows: mix the above-mentioned raw materials according to the above-mentioned ratio to obtain a mixed salt, and place it in a dry airtight container; heat the crucible to 130°C, add the mixed salt In the crucible, raise the temperature of the crucible to 825°C, and stir the mixed salt with a ladle during the heating process until the mixed salt is completely melted; after fully stirring the liquid mixed salt, pour it into the mold, solidify and cool to obtain a block flux; The flux is crushed, placed in a grinding bowl, crushed, and ground to obtain a powdery flux, which is sieved through a sieve with a mesh size of 10 to obtain refining agent B and stored in a dry airtight container for later use.
在使用上述得到的精炼剂B时,在刷有涂料的铁质坩埚中撒入覆盖剂,加入纯镁并升温至780℃,期间撒入覆盖剂阻燃,随后加入中间合金至熔体成分配比为Mg-2.8Nd-1.4Gd-0.4Zn-0.5Zr,搅拌至中间合金充分熔化;精炼时,一边搅拌合金液,一边加入1.5wt.%上述精炼剂,精炼时间为8分钟;精炼处理完毕后捞渣、静置30min后反重力铸造浇注树脂砂型大型铸件,本体取样T6抗拉强度280MPa,延伸率3%。When using the refining agent B obtained above, sprinkle the covering agent into the painted iron crucible, add pure magnesium and raise the temperature to 780°C, during which the covering agent is sprinkled to prevent flames, and then add the master alloy to the melt composition distribution The ratio is Mg-2.8Nd-1.4Gd-0.4Zn-0.5Zr, stir until the intermediate alloy is fully melted; when refining, add 1.5wt.% of the above refining agent while stirring the alloy liquid, and the refining time is 8 minutes; the refining process is completed After removing the slag and standing still for 30 minutes, reverse gravity casting and pouring resin sand mold large-scale castings. The body sampling T6 tensile strength is 280MPa, and the elongation is 3%.
实施例3Example 3
按下述步骤制备一种稀土镁合金用低泡少烟精炼剂,其组分和质量分数为:CaCl2:32%;BaCl2:12%;NaCl:2%;CaF2:3%;BaF2:8%;KF:19%;KCl:24%。Prepare a low-foaming and less-smoke refining agent for rare earth magnesium alloys according to the following steps, its components and mass fractions are: CaCl 2 : 32%; BaCl 2 : 12%; NaCl: 2%; CaF 2 : 3%; BaF 2 : 8%; KF: 19%; KCl: 24%.
本实施例的稀土镁合金用低泡少烟精炼剂制备步骤为:将上述原料按上述配比混合均匀后得到混合盐,置于干燥密闭容器内;将坩埚加热至120℃,将混合盐加入坩埚中,将坩埚升温至840℃,升温过程中用浇勺搅拌混合盐,直至混合盐完全熔化;将液态混合盐充分搅拌后,浇注到模具中,凝固冷却后得到块状熔剂;将块状熔剂破碎,置入研磨钵捣碎、碾磨,得到粉状熔剂,用筛孔目数为10目的筛子过筛后,得到精炼剂C放于干燥密闭容器备用。The preparation steps of the low-foaming and less-smoke refining agent for rare earth magnesium alloys in this example are as follows: mix the above-mentioned raw materials according to the above-mentioned ratio to obtain a mixed salt, and place it in a dry airtight container; heat the crucible to 120°C, add the mixed salt In the crucible, raise the temperature of the crucible to 840°C, stir the mixed salt with a spoon during the heating process, until the mixed salt is completely melted; after fully stirring the liquid mixed salt, pour it into the mold, solidify and cool to obtain a block flux; The flux is crushed, placed in a grinding bowl, crushed, and ground to obtain a powdery flux, which is sieved through a sieve with a mesh size of 10 to obtain refining agent C and stored in a dry airtight container for later use.
在使用上述得到的精炼剂C时,在刷有涂料的铁质坩埚中撒入覆盖剂,加入纯镁并升温至780℃,期间撒入覆盖剂阻燃,随后加入中间合金至熔体成分配比为Mg-6Gd-3Y-0.5Zr,搅拌至中间合金充分熔化;精炼时,一边搅拌合金液,一边加入2wt.%上述精炼剂,精炼时间为8分钟;精炼处理完毕后捞渣、静置30min后反重力铸造浇注树脂砂型大型铸件,本体取样T6抗拉强度332MPa,延伸率4.2%。When using the refining agent C obtained above, sprinkle the covering agent into the painted iron crucible, add pure magnesium and raise the temperature to 780°C, during which the covering agent is sprinkled to prevent flames, and then add the master alloy to the melt composition The ratio is Mg-6Gd-3Y-0.5Zr, stirring until the intermediate alloy is fully melted; during refining, while stirring the alloy liquid, add 2wt.% of the above-mentioned refining agent, and the refining time is 8 minutes; After 30 minutes, anti-gravity casting cast resin sand mold large castings, body sampling T6 tensile strength 332MPa, elongation 4.2%.
以上结合具体实施方式和范例性实例对本发明进行了详细说明,不过这些说明并不能理解为对本发明的限制。本领域技术人员理解,在不偏离本发明精神和范围的情况下,可以对本发明技术方案及其实施方式进行多种等价替换、修饰或改进,这些均落入本发明的范围内。本发明的保护范围以所附权利要求为准。The present invention has been described in detail above in conjunction with specific implementations and exemplary examples, but these descriptions should not be construed as limiting the present invention. Those skilled in the art understand that without departing from the spirit and scope of the present invention, various equivalent replacements, modifications or improvements can be made to the technical solutions and implementations of the present invention, all of which fall within the scope of the present invention. The protection scope of the present invention shall be determined by the appended claims.
本发明说明书中未作详细描述的内容属本领域技术人员的公知技术。The content that is not described in detail in the description of the present invention belongs to the well-known technology of those skilled in the art.
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